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CO4560557A1 - Proceso y unidad de retroajuste para la actualizacion de una planta de gas natural - Google Patents

Proceso y unidad de retroajuste para la actualizacion de una planta de gas natural

Info

Publication number
CO4560557A1
CO4560557A1 CO96056849A CO96056849A CO4560557A1 CO 4560557 A1 CO4560557 A1 CO 4560557A1 CO 96056849 A CO96056849 A CO 96056849A CO 96056849 A CO96056849 A CO 96056849A CO 4560557 A1 CO4560557 A1 CO 4560557A1
Authority
CO
Colombia
Prior art keywords
ngl
fractioning
train
unit
existing
Prior art date
Application number
CO96056849A
Other languages
English (en)
Inventor
R Mehra Yuv
Original Assignee
Advanced Extraction Technologies Inc
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 Advanced Extraction Technologies Inc filed Critical Advanced Extraction Technologies Inc
Publication of CO4560557A1 publication Critical patent/CO4560557A1/es

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1487—Removing organic compounds
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G5/00—Recovery of liquid hydrocarbon mixtures from gases, e.g. natural gas
    • C10G5/04—Recovery of liquid hydrocarbon mixtures from gases, e.g. natural gas with liquid absorbents
    • 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
    • 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
    • F25J2200/04—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
    • F25J2205/00—Processes or apparatus using other separation and/or other processing means
    • F25J2205/50—Processes or apparatus using other separation and/or other processing means using absorption, i.e. with selective solvents or lean oil, heavier CnHm and including generally a regeneration step for the solvent or lean oil
    • 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
    • F25J2215/00—Processes characterised by the type or other details of the product stream
    • F25J2215/64—Propane or propylene
    • 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
    • F25J2215/66—Butane or mixed butanes
    • 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
    • F25J2230/00—Processes or apparatus involving steps for increasing the pressure of gaseous process streams
    • F25J2230/08—Cold compressor, i.e. suction of the gas at cryogenic temperature and generally without afterstage-cooler
    • 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
    • F25J2230/00—Processes or apparatus involving steps for increasing the pressure of gaseous process streams
    • F25J2230/60—Processes or apparatus involving steps for increasing the pressure of gaseous process streams the fluid being hydrocarbons or 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
    • 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
    • F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
    • F25J2290/80—Retrofitting, revamping or debottlenecking of existing plant

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • Separation By Low-Temperature Treatments (AREA)
  • Gas Separation By Absorption (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

1. UNA UNIDAD RETROAJUSTADA A UNA PLANTA DE GAS NATURAL REFRIGERADO SIMPLE EXISTENTE QUE INCREMEN- TA SIGNIFICATIVAMENTE LA CANTIDAD DE PROPANO, BUTANOS Y GASOLINA NATUTRAL, O ETANO, PROPANO, BUTANOS, Y GASOLINA NATURAL RECUPERADOS A PARTIR DE GAS NATURAL DE LA PLANTA DE TRATAMIENTO DE GAS EXISTENTE, EN UNA DE CUYAS REALIZACIONES DE PLANTA DE TRATAMIENTO DE GAS NATURAL EXISTENTE INCLUYE UN ENFRIADOR DE ALIMENTACION REFRIGERADA, UN SEPARADOR Y UN ESTABILIZADSOR Y LA UNIDAD RETROAJUSTADDA COMPRENDE UN ABSORBENTE DE NGL, EN ENFRIADOR DE SOLVENTE POBRE REFRIGERADO Y UN REGENERADOR DE SOLVENTE POBRE; Y EN OTRA DE CUYAS REALIZACIONES LA PLANTA DE TRATAMIENTO DE GAS REFRIGERADO SIMPLE EXISTENTE ADEMAS INCLUYE TREN E DE FRACCIONAMIENTO DE NGL QUE SEPARA EL NGL RECUPERADO EN FRACCIONES COMERCIALIZABLES, Y CUYO TREN DE FRACCIONAMIENTO DE HGL QUE SEPARA EL HGL RECUPERADO EN FRACCCIONES COMERCIABLES, Y CUYO TREN DE FRACCIONAMIENTO DE NGL QUE SEPARA EL NGL RECUPERADO EN FRACCIONES COMERCIABLES, Y CUYO TREN DE FRACCIONAMIENTO DE NGL INCLUYE INCLUYE UN DEBUTANIZADOR QUE PRODUCE LA TOTALIDAD O UNA PARTE DE SOLVENTE POBRE UTILIZADO ENLA UNIDAD RETROAJUSTADA QUE COMPRENDE UN ABSORBENTE DE NGL QUE SEPARA EL NGL RECUPERADOEN FRACCIONES COMERCI- ALIZABLES, Y CUYO TREN DE FRACCIONAMIENTO DE NGL INCLUYE UN DEBUTINIZADOR QUE PRODUCE LA TOTALIDAD O LA PARTE DE SOLVENTE POBRE UTILIZADO EN LA UNIDAD RETROJUSTADA QUE COMPRENDE UN ABSORBENTE DE NGL INCLUYE UN DEBUTANIZADOR QUE PRODUCE LA TOTALIDAD O UNA PARTE DEL SOLVENTE REFRIGERADO; Y ENLA CUAL EL PROCESO DE TRATAMIENTO DE GAS NATURAL UTILIZA UN SOLVENTE PRESATURADO CON COMPONENTES MAS LIVIANOS INDESEABLES PRESENTES EN LA CORRIENTE DE LA PARTE SUPERIOR DEL ABSORBENTE DE NGL. * VER FIGURA O
CO96056849A 1995-10-27 1996-10-28 Proceso y unidad de retroajuste para la actualizacion de una planta de gas natural CO4560557A1 (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US08/549,276 US5561988A (en) 1995-10-27 1995-10-27 Retrofit unit for upgrading natural gas refrigeraition plants
US08/697,829 US5687584A (en) 1995-10-27 1996-08-30 Absorption process with solvent pre-saturation

Publications (1)

Publication Number Publication Date
CO4560557A1 true CO4560557A1 (es) 1998-02-10

Family

ID=24192336

Family Applications (1)

Application Number Title Priority Date Filing Date
CO96056849A CO4560557A1 (es) 1995-10-27 1996-10-28 Proceso y unidad de retroajuste para la actualizacion de una planta de gas natural

Country Status (5)

Country Link
US (2) US5561988A (es)
AR (1) AR004101A1 (es)
CA (1) CA2176430C (es)
CO (1) CO4560557A1 (es)
MY (1) MY119991A (es)

Families Citing this family (42)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6158241A (en) * 1998-01-01 2000-12-12 Erickson; Donald C. LPG recovery from reformer treat gas
EP1412682A1 (en) 2001-06-29 2004-04-28 ExxonMobil Upstream Research Company Process for recovering ethane and heavier hydrocarbons from a methane-rich pressurized liquid mixture
CN1205450C (zh) * 2001-08-23 2005-06-08 吕应中 天然气综合处理装置
US6740226B2 (en) * 2002-01-16 2004-05-25 Saudi Arabian Oil Company Process for increasing hydrogen partial pressure in hydroprocessing processes
US6941771B2 (en) * 2002-04-03 2005-09-13 Howe-Baker Engineers, Ltd. Liquid natural gas processing
US7475566B2 (en) * 2002-04-03 2009-01-13 Howe-Barker Engineers, Ltd. Liquid natural gas processing
US7357003B2 (en) * 2003-07-24 2008-04-15 Toyo Engineering Corporation Process and apparatus for separation of hydrocarbons
US7481858B2 (en) * 2005-02-25 2009-01-27 Societe Bic Hydrogen generating fuel cell cartridges
CN100565061C (zh) * 2003-10-30 2009-12-02 弗劳尔科技公司 柔性液态天然气工艺和方法
CA2544428C (en) * 2003-11-03 2009-06-02 Fluor Technologies Corporation Lng vapor handling configurations and methods
RU2366872C2 (ru) * 2004-03-11 2009-09-10 Эдванст Экстрэкшн Текнолоджиз, Инк. Использование криогенных температур при обработке газов, содержащих легкие компоненты, с помощью физических растворителей
US7159417B2 (en) * 2004-03-18 2007-01-09 Abb Lummus Global, Inc. Hydrocarbon recovery process utilizing enhanced reflux streams
US7165423B2 (en) * 2004-08-27 2007-01-23 Amec Paragon, Inc. Process for extracting ethane and heavier hydrocarbons from LNG
MY138093A (en) * 2004-11-04 2009-04-30 Ngl Technologies Sdn Bhd Process for extracting natural gas liquids from natural gas
EP1880001B1 (en) * 2005-05-31 2011-06-08 The Iams Company Feline probiotic lactobacilli
US9017547B2 (en) * 2005-07-20 2015-04-28 Saudi Arabian Oil Company Hydrogen purification for make-up gas in hydroprocessing processes
AU2007273015B2 (en) * 2006-07-10 2010-06-10 Fluor Technologies Corporation Configurations and methods for rich gas conditioning for NGL recovery
RU2379085C2 (ru) * 2006-07-31 2010-01-20 Юрий Григорьевич Белостоцкий Способ абсорбционной конденсации паров легкокипящей жидкости и устройство для абсорбционной конденсации паров легкокипящей жидкости
US9574823B2 (en) * 2007-05-18 2017-02-21 Pilot Energy Solutions, Llc Carbon dioxide recycle process
US9255731B2 (en) 2007-05-18 2016-02-09 Pilot Energy Solutions, Llc Sour NGL stream recovery
US8505332B1 (en) * 2007-05-18 2013-08-13 Pilot Energy Solutions, Llc Natural gas liquid recovery process
US9752826B2 (en) 2007-05-18 2017-09-05 Pilot Energy Solutions, Llc NGL recovery from a recycle stream having natural gas
US9200833B2 (en) 2007-05-18 2015-12-01 Pilot Energy Solutions, Llc Heavy hydrocarbon processing in NGL recovery system
RU2370300C1 (ru) * 2008-03-11 2009-10-20 Юрий Григорьевич Белостоцкий Способ абсорбционной конденсации паров легкокипящей жидкости и устройство для реализации такого способа
US20100281914A1 (en) * 2009-05-07 2010-11-11 Dew Point Control, Llc Chilled water skid for natural gas processing
US10451344B2 (en) 2010-12-23 2019-10-22 Fluor Technologies Corporation Ethane recovery and ethane rejection methods and configurations
WO2014047464A1 (en) 2012-09-20 2014-03-27 Fluor Technologies Corporation Configurations and methods for ngl recovery for high nitrogen content feed gases
US20140366577A1 (en) * 2013-06-18 2014-12-18 Pioneer Energy Inc. Systems and methods for separating alkane gases with applications to raw natural gas processing and flare gas capture
US20160187057A1 (en) * 2014-12-23 2016-06-30 Aspen Engineering Services, Llc Liquefied natural gas from rich natural gas
US10006701B2 (en) 2016-01-05 2018-06-26 Fluor Technologies Corporation Ethane recovery or ethane rejection operation
US10330382B2 (en) 2016-05-18 2019-06-25 Fluor Technologies Corporation Systems and methods for LNG production with propane and ethane recovery
WO2018049128A1 (en) 2016-09-09 2018-03-15 Fluor Technologies Corporation Methods and configuration for retrofitting ngl plant for high ethane recovery
CN106753635B (zh) * 2016-12-06 2019-05-03 河北工业大学 同时处理天然气和凝析油回收液化气和乙二醇的生产方法及设备
WO2018175388A1 (en) * 2017-03-20 2018-09-27 Conocophillips Company Alternative two column hru design with rich reflux
WO2019078892A1 (en) 2017-10-20 2019-04-25 Fluor Technologies Corporation IMPLEMENTATION BY PHASES OF RECOVERY PLANTS OF NATURAL GAS LIQUIDS
CN109028758A (zh) * 2018-08-07 2018-12-18 中国石油工程建设有限公司 一种采用混合冷剂制冷的天然气乙烷回收装置及方法
US12215922B2 (en) 2019-05-23 2025-02-04 Fluor Technologies Corporation Integrated heavy hydrocarbon and BTEX removal in LNG liquefaction for lean gases
US12098882B2 (en) 2018-12-13 2024-09-24 Fluor Technologies Corporation Heavy hydrocarbon and BTEX removal from pipeline gas to LNG liquefaction
RU2715772C1 (ru) * 2019-09-02 2020-03-03 Владимир Александрович Чигряй Газоперерабатывающий кластер
US12110460B2 (en) * 2019-10-28 2024-10-08 China Petroleum & Chemical Corporation Method and apparatus for recovering C2—C4 components in methane-containing industrial gas
RU2771006C1 (ru) * 2021-05-31 2022-04-25 Игорь Анатольевич Мнушкин Комплекс переработки в газохимическую продукцию углеводородного сырья месторождений, расположенных в сложных климатических условиях
US12234421B2 (en) 2021-08-27 2025-02-25 Pilot Intellectual Property, Llc Carbon dioxide recycle stream processing with ethylene glycol dehydrating in an enhanced oil recovery process

Family Cites Families (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2337254A (en) * 1940-08-02 1943-12-21 Phillips Petroleum Co Method of recovering hydrocarbons
US2335162A (en) * 1941-06-02 1943-11-23 Shell Dev Process for the separation of hydrocarbon gases
US2377736A (en) * 1942-01-23 1945-06-05 Universal Oil Prod Co Fractionation of hydrocarbons
US2428521A (en) * 1945-12-17 1947-10-07 Phillips Petroleum Co Recovery of ethane and gasoline from natural gas
NL68945C (es) * 1946-11-04
US2516507A (en) * 1947-03-29 1950-07-25 Shell Dev Absorption separation process for hydrocarbons
US2666019A (en) * 1950-07-28 1954-01-12 Socony Vacuum Oil Co Inc Method for recovering propane and heavier hydrocarbons
US2782141A (en) * 1953-02-09 1957-02-19 Union Oil Co Absorption process
US2849371A (en) * 1954-09-27 1958-08-26 Phillips Petroleum Co Separation and recovery of hydrocarbons from gaseous mixtures thereof
US2857018A (en) * 1956-09-27 1958-10-21 Kellogg M W Co Gas separation
US2959540A (en) * 1958-12-02 1960-11-08 Exxon Research Engineering Co Light ends absorption system
US3214890A (en) * 1962-04-19 1965-11-02 Marathon Oil Co Method of separation of hydrocarbons by a single absorption oil
US4072604A (en) * 1974-03-21 1978-02-07 Uop Inc. Process to separate hydrocarbons from gas streams
US4692179A (en) * 1982-05-03 1987-09-08 Advanced Extraction Technologies, Inc. Process for using alkyl substituted C8-C10 aromatic hydrocarbons as preferential physical solvents for selective processing of hydrocarbon gas streams
US4883515A (en) * 1982-05-03 1989-11-28 Advanced Extraction Technologies, Inc. Processing hydrocarbon gases with selected physical solvents
FR2544998B1 (fr) * 1983-04-29 1985-07-19 Inst Francais Du Petrole Nouveau procede de fractionnement d'un melange gazeux de plusieurs constituants
DE3408760A1 (de) * 1984-03-09 1985-09-12 Linde Ag, 6200 Wiesbaden Verfahren zur gewinnung von c(pfeil abwaerts)3(pfeil abwaerts)(pfeil abwaerts)+(pfeil abwaerts)-kohlenwasserstoffen
DE3445961A1 (de) * 1984-12-17 1986-06-26 Linde Ag, 6200 Wiesbaden Verfahren zur abtrennung von c(pfeil abwaerts)3(pfeil abwaerts)(pfeil abwaerts)+(pfeil abwaerts)-kohlenwasserstoffen aus einem gasstrom
US4617038A (en) * 1985-07-26 1986-10-14 El Paso Hydrocarbons Company Process for using preferential physical solvents for selective processing of hydrocarbon gas streams
US4696688A (en) * 1985-12-13 1987-09-29 Advanced Extraction Technologies, Inc. Conversion of lean oil absorption process to extraction process for conditioning natural gas
DE3539554A1 (de) * 1985-11-07 1987-05-14 Linde Ag Verfahren zum gewinnen von c(pfeil abwaerts)2(pfeil abwaerts)(pfeil abwaerts)+(pfeil abwaerts) oder c(pfeil abwaerts)3(pfeil abwaerts)(pfeil abwaerts)+(pfeil abwaerts)-kohlenwasserstoffen aus gasgemischen
US5345772A (en) * 1993-05-14 1994-09-13 Process Systems International, Inc. Single column distillative separation employing bottom additives
US5462583A (en) * 1994-03-04 1995-10-31 Advanced Extraction Technologies, Inc. Absorption process without external solvent

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CA2176430A1 (en) 1997-04-28
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US5687584A (en) 1997-11-18
US5561988A (en) 1996-10-08
AR004101A1 (es) 1998-09-30

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