AR023066A1 - Proceso para la separacion de un flujo de gas - Google Patents

Proceso para la separacion de un flujo de gas

Info

Publication number
AR023066A1
AR023066A1 ARP990106118A ARP990106118A AR023066A1 AR 023066 A1 AR023066 A1 AR 023066A1 AR P990106118 A ARP990106118 A AR P990106118A AR P990106118 A ARP990106118 A AR P990106118A AR 023066 A1 AR023066 A1 AR 023066A1
Authority
AR
Argentina
Prior art keywords
tower
components
flow
kettle
column
Prior art date
Application number
ARP990106118A
Other languages
English (en)
Original Assignee
Ortloff Engineers Ltd
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 Ortloff Engineers Ltd filed Critical Ortloff Engineers Ltd
Publication of AR023066A1 publication Critical patent/AR023066A1/es

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
    • F25J3/0228—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
    • F25J3/0204—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
    • F25J3/0204—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
    • F25J3/0219—Refinery gas, cracking gas, coke oven gas, gaseous mixtures containing aliphatic unsaturated CnHm or gaseous mixtures of undefined nature
    • 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
    • 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
    • F25J2200/30—Processes or apparatus using separation by rectification using a side column in a single pressure 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
    • F25J2200/70—Refluxing the column with a condensed part of the feed stream, i.e. fractionator top is stripped or self-rectified
    • 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
    • F25J2200/76—Refluxing the column with condensed overhead gas being cycled in a quasi-closed loop refrigeration 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
    • F25J2200/00—Processes or apparatus using separation by rectification
    • F25J2200/90—Details relating to column internals, e.g. structured packing, gas or liquid distribution
    • 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
    • F25J2210/00—Processes characterised by the type or other details of the feed stream
    • F25J2210/12—Refinery or petrochemical off-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
    • F25J2220/00—Processes or apparatus involving steps for the removal of impurities
    • F25J2220/60—Separating impurities from natural gas, e.g. mercury, cyclic hydrocarbons
    • F25J2220/66—Separating acid gases, e.g. CO2, SO2, H2S or RSH
    • 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
    • F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
    • F25J2290/40—Vertical layout or arrangement of cold equipments within in the cold box, e.g. columns, condensers, heat exchangers etc.
    • 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
    • Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00—Capture or disposal of greenhouse gases
    • Y02C20/40—Capture or disposal of greenhouse gases of CO2

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Separation By Low-Temperature Treatments (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Separation Of Gases By Adsorption (AREA)

Abstract

Se divulga un proceso para la recuperacion de etano, etileno, propano, propileno y componentes hidrocarburicos más pesados a partir de un flujo de gas dehidrocarburo. En anos recientes, el método recomendado para separar un flujo de gas de hidrocarburo por lo general ha incluido suministrar al menos porcionesdel flujo de gas a una torre de fraccionamiento que tiene al menos un hervidor, y a menudo uno o más hervidores laterales, para proporcionar calor a la columnaretirando y calentando parted e los líquidos de la torre para producir vapores separadores que dividen los componentes más volátiles de los componentesdeseados. El hervidor y los hervidores laterales (si los hubiera) generalmente están integrados en el esquema de enfriamientode flujo de alimentacion paraproporcionar al menos una porcion de la refrigeracion necesaria para condensar los componentes deseados para un posterior fraccionamiento en la columna dedestilacion. En el proceso que se divulga, el esquema de hervidorde l a torre se ha modificado para usar uno o más flujos de destilacion de líquido de la torredesde un punto más alto en la columna del que se usa en el esquema de hervidor convencional, proporcionando un flujo (o flujos) de menor temperaturaalhervidor, lo cual permite un enfriamiento más efectivo de los flujos de alimentacion y de este modo mejora la eficacia con la cual se recuperan los componentes. Asimismo, los flujos de líquido de la torre que se retiran desde un punto más alto enla columna co ntienen mayores cantidades de componentes más volátiles,que cuando se vaporizan proporcionan una mejor separacion de los componentes indeseables como dioxido de carbono, sin reducir la recuperacion de loscomponentes deseados. El flujode destilacion calentado regresa a un punto inferior en la torre de fraccionamiento que está separado del punto de extraccion almenos en una fase teorica.
ARP990106118A 1998-12-01 1999-12-01 Proceso para la separacion de un flujo de gas AR023066A1 (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US11050298P 1998-12-01 1998-12-01
US09/439,508 US6182469B1 (en) 1998-12-01 1999-11-12 Hydrocarbon gas processing

Publications (1)

Publication Number Publication Date
AR023066A1 true AR023066A1 (es) 2002-09-04

Family

ID=26808081

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP990106118A AR023066A1 (es) 1998-12-01 1999-12-01 Proceso para la separacion de un flujo de gas

Country Status (20)

Country Link
US (1) US6182469B1 (es)
EP (1) EP1137903B1 (es)
CN (1) CN1154830C (es)
AR (1) AR023066A1 (es)
AT (1) ATE295519T1 (es)
AU (1) AU751881B2 (es)
BR (1) BR9915807A (es)
CA (1) CA2351423C (es)
CO (1) CO5100991A1 (es)
DE (1) DE69925306D1 (es)
EA (1) EA003854B1 (es)
EG (1) EG22416A (es)
ID (1) ID29883A (es)
MY (1) MY125613A (es)
NO (1) NO322415B1 (es)
PE (1) PE20001473A1 (es)
SA (1) SA00201021B1 (es)
TW (1) TW512142B (es)
UA (1) UA46176C2 (es)
WO (1) WO2000033006A1 (es)

Families Citing this family (125)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6278035B1 (en) * 2000-03-17 2001-08-21 Ronald D. Key Process for C2 recovery
AU7158701A (en) * 2000-08-11 2002-02-25 Fluor Corp High propane recovery process and configurations
CN100451507C (zh) * 2000-10-02 2009-01-14 奥鲁工程有限公司 烃类气体的加工方法
US6367286B1 (en) * 2000-11-01 2002-04-09 Black & Veatch Pritchard, Inc. System and process for liquefying high pressure natural gas
US6712880B2 (en) 2001-03-01 2004-03-30 Abb Lummus Global, Inc. Cryogenic process utilizing high pressure absorber column
US6526777B1 (en) 2001-04-20 2003-03-04 Elcor Corporation LNG production in cryogenic natural gas processing plants
UA76750C2 (uk) * 2001-06-08 2006-09-15 Елккорп Спосіб зрідження природного газу (варіанти)
US6742358B2 (en) * 2001-06-08 2004-06-01 Elkcorp Natural gas liquefaction
US6516631B1 (en) 2001-08-10 2003-02-11 Mark A. Trebble Hydrocarbon gas processing
FR2831656B1 (fr) * 2001-10-31 2004-04-30 Technip Cie Procede et installation de separation d'un gaz contenant du methane et de l'ethane a deux colonnes fonctionnant sous deux pressions differentes
CN100408954C (zh) * 2001-11-09 2008-08-06 弗劳尔公司 提高ngl回收率的装置和方法
US6823692B1 (en) 2002-02-11 2004-11-30 Abb Lummus Global Inc. Carbon dioxide reduction scheme for NGL processes
US6941771B2 (en) * 2002-04-03 2005-09-13 Howe-Baker Engineers, Ltd. Liquid natural gas processing
DE60220954T2 (de) * 2002-05-08 2008-02-28 Fluor Corp., Aliso Viejo Konfiguration und verfahren zur gewinnung von flüssigem erdgas unter verwendung eines unterkühlten rückflussverfahrens
EP1508010B1 (en) * 2002-05-20 2008-01-09 Fluor Corporation Twin reflux process and configurations for improved natural gas liquids recovery
EA008393B1 (ru) * 2002-08-15 2007-04-27 Флуор Корпорейшн Установка сжиженного природного газа низкого давления
US6945075B2 (en) * 2002-10-23 2005-09-20 Elkcorp Natural gas liquefaction
US7069744B2 (en) * 2002-12-19 2006-07-04 Abb Lummus Global Inc. Lean reflux-high hydrocarbon recovery process
US7484385B2 (en) * 2003-01-16 2009-02-03 Lummus Technology Inc. Multiple reflux stream hydrocarbon recovery process
JP4571934B2 (ja) * 2003-02-25 2010-10-27 オートロフ・エンジニアーズ・リミテッド 炭化水素ガス処理
US6889523B2 (en) 2003-03-07 2005-05-10 Elkcorp LNG production in cryogenic natural gas processing plants
US7107788B2 (en) * 2003-03-07 2006-09-19 Abb Lummus Global, Randall Gas Technologies Residue recycle-high ethane recovery process
US7155931B2 (en) * 2003-09-30 2007-01-02 Ortloff Engineers, Ltd. Liquefied natural gas processing
JP4599362B2 (ja) * 2003-10-30 2010-12-15 フルオー・テクノロジーズ・コーポレイシヨン 自在ｎｇｌプロセスおよび方法
US7159417B2 (en) * 2004-03-18 2007-01-09 Abb Lummus Global, Inc. Hydrocarbon recovery process utilizing enhanced reflux streams
US7204100B2 (en) * 2004-05-04 2007-04-17 Ortloff Engineers, Ltd. Natural gas liquefaction
KR101200611B1 (ko) * 2004-07-01 2012-11-12 오르트로프 엔지니어스, 리미티드 액화 천연 가스 처리
RU2272973C1 (ru) * 2004-09-24 2006-03-27 Салават Зайнетдинович Имаев Способ низкотемпературной сепарации газа (варианты)
US20060130521A1 (en) * 2004-12-17 2006-06-22 Abb Lummus Global Inc. Method for recovery of natural gas liquids for liquefied natural gas
US20060130520A1 (en) * 2004-12-17 2006-06-22 Abb Lummus Global Inc. Method for recovery of natural gas liquids for liquefied natural gas
NZ556495A (en) * 2005-02-24 2009-09-25 Twister Bv Method and system for cooling a natural gas stream and separating the cooled stream into various fractions
US9080810B2 (en) * 2005-06-20 2015-07-14 Ortloff Engineers, Ltd. Hydrocarbon gas processing
EA014452B1 (ru) * 2005-07-07 2010-12-30 Флуор Текнолоджиз Корпорейшн Способы и установка для извлечения газоконденсатных жидкостей
WO2007116050A2 (en) * 2006-04-12 2007-10-18 Shell Internationale Research Maatschappij B.V. Method and apparatus for liquefying a natural gas stream
CN101460800B (zh) * 2006-06-02 2012-07-18 奥特洛夫工程有限公司 液化天然气的处理
EA013423B1 (ru) * 2006-06-27 2010-04-30 Флуор Текнолоджиз Корпорейшн Способ и система извлечения этана
WO2008008335A2 (en) * 2006-07-10 2008-01-17 Fluor Technologies Corporation Configurations and methods for rich gas conditioning for ngl recovery
BRPI0717384A2 (pt) * 2006-10-24 2013-10-15 Shell Int Research Método e aparelho para o tratamento de uma corrente de hidrocarbonetos
US7777088B2 (en) * 2007-01-10 2010-08-17 Pilot Energy Solutions, Llc Carbon dioxide fractionalization process
US8590340B2 (en) * 2007-02-09 2013-11-26 Ortoff Engineers, Ltd. Hydrocarbon gas processing
US9869510B2 (en) * 2007-05-17 2018-01-16 Ortloff Engineers, Ltd. Liquefied natural gas processing
US8919148B2 (en) * 2007-10-18 2014-12-30 Ortloff Engineers, Ltd. Hydrocarbon gas processing
US9243842B2 (en) 2008-02-15 2016-01-26 Black & Veatch Corporation Combined synthesis gas separation and LNG production method and system
US8973398B2 (en) 2008-02-27 2015-03-10 Kellogg Brown & Root Llc Apparatus and method for regasification of liquefied natural gas
US8640494B2 (en) * 2008-05-15 2014-02-04 Jose Lourenco Method to produce natural gas liquids NGLs at gas Pressure Reduction Stations
US20090282865A1 (en) 2008-05-16 2009-11-19 Ortloff Engineers, Ltd. Liquefied Natural Gas and Hydrocarbon Gas Processing
US20090293537A1 (en) * 2008-05-27 2009-12-03 Ameringer Greg E NGL Extraction From Natural Gas
JP2011522381A (ja) * 2008-05-30 2011-07-28 コロラド ステート ユニバーシティ リサーチ ファンデーション プラズマに基づく化学源装置およびその使用方法
US8994270B2 (en) 2008-05-30 2015-03-31 Colorado State University Research Foundation System and methods for plasma application
US9272359B2 (en) 2008-05-30 2016-03-01 Colorado State University Research Foundation Liquid-gas interface plasma device
JP2011521735A (ja) * 2008-05-30 2011-07-28 コロラド ステート ユニバーシティ リサーチ ファンデーション プラズマを発生させるためのシステム、方法、および装置
US9028656B2 (en) 2008-05-30 2015-05-12 Colorado State University Research Foundation Liquid-gas interface plasma device
CN101290184B (zh) * 2008-06-05 2010-10-13 北京国能时代能源科技发展有限公司 一种化工尾气的液化分离方法及设备
US8381544B2 (en) * 2008-07-18 2013-02-26 Kellogg Brown & Root Llc Method for liquefaction of natural gas
US8584488B2 (en) * 2008-08-06 2013-11-19 Ortloff Engineers, Ltd. Liquefied natural gas production
US20100050688A1 (en) * 2008-09-03 2010-03-04 Ameringer Greg E NGL Extraction from Liquefied Natural Gas
EP2350546A1 (en) * 2008-10-07 2011-08-03 Exxonmobil Upstream Research Company Helium recovery from natural gas integrated with ngl recovery
EP2364413B1 (en) * 2008-11-10 2016-06-15 1304338 Alberta Ltd Method to increase gas mass flow injection rates to gas storage caverns using lng
US9052137B2 (en) 2009-02-17 2015-06-09 Ortloff Engineers, Ltd. Hydrocarbon gas processing
US9074814B2 (en) * 2010-03-31 2015-07-07 Ortloff Engineers, Ltd. Hydrocarbon gas processing
US9933207B2 (en) * 2009-02-17 2018-04-03 Ortloff Engineers, Ltd. Hydrocarbon gas processing
MX341798B (es) * 2009-02-17 2016-09-02 Ortloff Engineers Ltd Procesamiento de gases de hidrocarburos.
US9939195B2 (en) * 2009-02-17 2018-04-10 Ortloff Engineers, Ltd. Hydrocarbon gas processing including a single equipment item processing assembly
US9080811B2 (en) * 2009-02-17 2015-07-14 Ortloff Engineers, Ltd Hydrocarbon gas processing
US8881549B2 (en) * 2009-02-17 2014-11-11 Ortloff Engineers, Ltd. Hydrocarbon gas processing
US9052136B2 (en) * 2010-03-31 2015-06-09 Ortloff Engineers, Ltd. Hydrocarbon gas processing
US20100287982A1 (en) 2009-05-15 2010-11-18 Ortloff Engineers, Ltd. Liquefied Natural Gas and Hydrocarbon Gas Processing
US8434325B2 (en) 2009-05-15 2013-05-07 Ortloff Engineers, Ltd. Liquefied natural gas and hydrocarbon gas processing
EA201200006A1 (ru) * 2009-06-11 2012-05-30 Ортлофф Инджинирс, Лтд. Переработка углеводородного газа
US20110067443A1 (en) * 2009-09-21 2011-03-24 Ortloff Engineers, Ltd. Hydrocarbon Gas Processing
US8222822B2 (en) 2009-10-27 2012-07-17 Tyco Healthcare Group Lp Inductively-coupled plasma device
US9021832B2 (en) 2010-01-14 2015-05-05 Ortloff Engineers, Ltd. Hydrocarbon gas processing
US9057558B2 (en) * 2010-03-31 2015-06-16 Ortloff Engineers, Ltd. Hydrocarbon gas processing including a single equipment item processing assembly
US9068774B2 (en) * 2010-03-31 2015-06-30 Ortloff Engineers, Ltd. Hydrocarbon gas processing
US9562717B2 (en) 2010-03-25 2017-02-07 The University Of Manchester Refrigeration process
US10113127B2 (en) 2010-04-16 2018-10-30 Black & Veatch Holding Company Process for separating nitrogen from a natural gas stream with nitrogen stripping in the production of liquefied natural gas
AU2011261670B2 (en) * 2010-06-03 2014-08-21 Uop Llc Hydrocarbon gas processing
WO2012075266A2 (en) 2010-12-01 2012-06-07 Black & Veatch Corporation Ngl recovery from natural gas using a mixed refrigerant
US10451344B2 (en) 2010-12-23 2019-10-22 Fluor Technologies Corporation Ethane recovery and ethane rejection methods and configurations
CA2728716C (en) * 2011-01-18 2017-12-05 Jose Lourenco Method of recovery of natural gas liquids from natural gas at ngls recovery plants
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.
US9683776B2 (en) * 2012-02-16 2017-06-20 Kellogg Brown & Root Llc Systems and methods for separating hydrocarbons using one or more dividing wall columns
US10139157B2 (en) 2012-02-22 2018-11-27 Black & Veatch Holding Company NGL recovery from natural gas using a mixed refrigerant
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
WO2014036322A1 (en) * 2012-08-30 2014-03-06 Fluor Technologies Corporation Configurations and methods for offshore ngl recovery
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
DE102013200572A1 (de) * 2013-01-16 2014-07-17 Siemens Aktiengesellschaft Vorrichtung zur Regasifizierung von Flüssigerdgas und zugehöriges Verfahren
US9532826B2 (en) 2013-03-06 2017-01-03 Covidien Lp System and method for sinus surgery
US9555145B2 (en) 2013-03-13 2017-01-31 Covidien Lp System and method for biofilm remediation
CA2813260C (en) 2013-04-15 2021-07-06 Mackenzie Millar A method to produce lng
US9581385B2 (en) 2013-05-15 2017-02-28 Linde Engineering North America Inc. Methods for separating hydrocarbon 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
US9783470B2 (en) 2013-09-11 2017-10-10 Ortloff Engineers, Ltd. Hydrocarbon gas processing
WO2015038288A1 (en) 2013-09-11 2015-03-19 Ortloff Engineers, Ltd. Hydrocarbon processing
AU2014318270B2 (en) 2013-09-11 2018-04-19 Uop Llc Hydrocarbon gas processing
US10563913B2 (en) 2013-11-15 2020-02-18 Black & Veatch Holding Company Systems and methods for hydrocarbon refrigeration with a mixed refrigerant cycle
US9574822B2 (en) 2014-03-17 2017-02-21 Black & Veatch Corporation Liquefied natural gas facility employing an optimized mixed refrigerant system
WO2015158395A1 (en) * 2014-04-17 2015-10-22 Statoil Petroleum As Extraction of natural gas liquids and cooling of treated recompressed gas
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
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
RU2576704C1 (ru) * 2015-04-20 2016-03-10 Андрей Владиславович Курочкин Способ подготовки углеводородного газа
RU2585333C1 (ru) * 2015-04-20 2016-05-27 Андрей Владиславович Курочкин Способ подготовки попутного нефтяного газа
CA2997628C (en) 2015-09-16 2022-10-25 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
DE102016003305A1 (de) * 2016-03-17 2017-09-21 Linde Aktiengesellschaft Verfahren zum Abtrennen einer ethanreichen Fraktion aus Erdgas
US10330382B2 (en) 2016-05-18 2019-06-25 Fluor Technologies Corporation Systems and methods for LNG production with propane and ethane recovery
US10533794B2 (en) 2016-08-26 2020-01-14 Ortloff Engineers, Ltd. Hydrocarbon gas processing
US10551119B2 (en) 2016-08-26 2020-02-04 Ortloff Engineers, Ltd. Hydrocarbon gas processing
US10551118B2 (en) 2016-08-26 2020-02-04 Ortloff Engineers, Ltd. Hydrocarbon gas processing
US11725879B2 (en) 2016-09-09 2023-08-15 Fluor Technologies Corporation Methods and configuration for retrofitting NGL plant for high ethane recovery
US11428465B2 (en) 2017-06-01 2022-08-30 Uop Llc Hydrocarbon gas processing
US11543180B2 (en) 2017-06-01 2023-01-03 Uop Llc Hydrocarbon gas processing
US11015865B2 (en) 2018-08-27 2021-05-25 Bcck Holding Company System and method for natural gas liquid production with flexible ethane recovery or rejection
US12098882B2 (en) 2018-12-13 2024-09-24 Fluor Technologies Corporation Heavy hydrocarbon and BTEX removal from pipeline gas to LNG liquefaction
CA3132386A1 (en) 2019-03-11 2020-09-17 Uop Llc Hydrocarbon gas processing
CN110118468B (zh) * 2019-05-10 2020-02-11 西南石油大学 一种带自冷循环适用于富气的乙烷回收方法
EP3771872A1 (de) * 2019-08-02 2021-02-03 Linde GmbH Verfahren und anlage zur bereitstellung eines erdgasprodukts
US11643604B2 (en) * 2019-10-18 2023-05-09 Uop Llc Hydrocarbon gas processing
WO2022005270A1 (en) * 2020-07-01 2022-01-06 Drl Engineering Sdn Bhd Split deethaniser fractionation
CN112452095B (zh) * 2020-11-10 2022-11-08 中国石油化工股份有限公司 一种改进的尾气精馏方法
FR3127558B1 (fr) * 2022-07-29 2024-07-19 Air Liquide Procédé et appareil de séparation à basse température d’un gaz contenant du CO2 pour produire un fluide riche en CO2
WO2023222637A1 (fr) * 2022-05-18 2023-11-23 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Procédé et appareil de séparation à basse température d'un gaz contenant du co2 pour produire un fluide riche en co2

Family Cites Families (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4171964A (en) 1976-06-21 1979-10-23 The Ortloff Corporation Hydrocarbon gas processing
US4157904A (en) 1976-08-09 1979-06-12 The Ortloff Corporation Hydrocarbon gas processing
US4251249A (en) 1977-01-19 1981-02-17 The Randall Corporation Low temperature process for separating propane and heavier hydrocarbons from a natural gas stream
US4185978A (en) 1977-03-01 1980-01-29 Standard Oil Company (Indiana) Method for cryogenic separation of carbon dioxide from hydrocarbons
US4278457A (en) 1977-07-14 1981-07-14 Ortloff Corporation Hydrocarbon gas processing
USRE33408E (en) 1983-09-29 1990-10-30 Exxon Production Research Company Process for LPG recovery
US4519824A (en) 1983-11-07 1985-05-28 The Randall Corporation Hydrocarbon gas separation
FR2571129B1 (fr) 1984-09-28 1988-01-29 Technip Cie Procede et installation de fractionnement cryogenique de charges gazeuses
US4617039A (en) 1984-11-19 1986-10-14 Pro-Quip Corporation Separating hydrocarbon gases
FR2578637B1 (fr) 1985-03-05 1987-06-26 Technip Cie Procede de fractionnement de charges gazeuses et installation pour l'execution de ce procede
US4687499A (en) 1986-04-01 1987-08-18 Mcdermott International Inc. Process for separating hydrocarbon gas constituents
US4710214A (en) * 1986-12-19 1987-12-01 The M. W. Kellogg Company Process for separation of hydrocarbon gases
US4869740A (en) 1988-05-17 1989-09-26 Elcor Corporation Hydrocarbon gas processing
US4854955A (en) 1988-05-17 1989-08-08 Elcor Corporation Hydrocarbon gas processing
US4889545A (en) 1988-11-21 1989-12-26 Elcor Corporation Hydrocarbon gas processing
US4895584A (en) * 1989-01-12 1990-01-23 Pro-Quip Corporation Process for C2 recovery
US5275005A (en) 1992-12-01 1994-01-04 Elcor Corporation Gas processing
US5568737A (en) 1994-11-10 1996-10-29 Elcor Corporation Hydrocarbon gas processing
US5566554A (en) * 1995-06-07 1996-10-22 Kti Fish, Inc. Hydrocarbon gas separation process
WO1996040604A1 (en) 1995-06-07 1996-12-19 Elcor Corporation Hydrocarbon gas processing
US5555748A (en) 1995-06-07 1996-09-17 Elcor Corporation Hydrocarbon gas processing
US5799507A (en) 1996-10-25 1998-09-01 Elcor Corporation Hydrocarbon gas processing
US5983664A (en) 1997-04-09 1999-11-16 Elcor Corporation Hydrocarbon gas processing
US5890378A (en) 1997-04-21 1999-04-06 Elcor Corporation Hydrocarbon gas processing
US5881569A (en) 1997-05-07 1999-03-16 Elcor Corporation Hydrocarbon gas processing

Also Published As

Publication number Publication date
AU751881B2 (en) 2002-08-29
SA00201021B1 (ar) 2006-05-28
NO322415B1 (no) 2006-10-02
EP1137903B1 (en) 2005-05-11
AU2031600A (en) 2000-06-19
MY125613A (en) 2006-08-30
DE69925306D1 (de) 2005-06-16
EA003854B1 (ru) 2003-10-30
CN1154830C (zh) 2004-06-23
ATE295519T1 (de) 2005-05-15
WO2000033006A1 (en) 2000-06-08
TW512142B (en) 2002-12-01
EP1137903A1 (en) 2001-10-04
UA46176C2 (uk) 2002-05-15
NO20012672L (no) 2001-07-18
CN1329709A (zh) 2002-01-02
CA2351423A1 (en) 2000-06-08
ID29883A (id) 2001-10-18
EG22416A (en) 2003-01-29
US6182469B1 (en) 2001-02-06
NO20012672D0 (no) 2001-05-31
BR9915807A (pt) 2001-08-21
CA2351423C (en) 2004-05-11
EA200100598A1 (ru) 2001-12-24
PE20001473A1 (es) 2000-12-25
CO5100991A1 (es) 2001-11-27

Similar Documents

Publication Publication Date Title
AR023066A1 (es) Proceso para la separacion de un flujo de gas
AR031133A1 (es) Procesamiento de gas de hidrocarburo
BRPI0414929A (pt) processamento de gás natural liquefeito
UY24761A1 (es) Procesamiento de gas de hidrocarburo
EA021947B1 (ru) Переработка углеводородного газа
CO5040108A1 (es) Proceso y aparato para la separacion de un flujo de gas que contiene hidrocarburo
CO6311034A2 (es) Procesamiento integrado de gas natural licuado y corrientes de gas de hidrocarburo para recuperar hidrocarburos mas pesados
JP7202388B2 (ja) 異性化ユニットにおける上部分割壁の使用
ES2284429T1 (es) Procesamiento de gas natural licuado.
EA014746B1 (ru) Установка и способ сепарации конденсата газа из углеводородных смесей высокого давления
NO337141B1 (no) Hydrokarbon gassbehandling for fete gasstrømmer
TW201541042A (zh) 於單一管柱設計中執行吸收／蒸餾的方法
NO316360B1 (no) Fremgangsmåte for behandling av naturgass inneholdende vann og kondenserbare hydrokarboner, samt anvendelse av slik fremgangsmåte
KR930003951A (ko) C₂+탄화수소 또는 c₃+탄화수소를 회수하는 방법
ECSP993247A (es) Procesamiento de gas de hidrocarburo
MY161443A (en) Hydrocarbon gas processing
MY158312A (en) Hydrocarbon gas processing
ECSP972292A (es) Procedimiento de gas de hidrocarburo
TH62370A (th) การดำเนินกระบวนการก๊าซไฮโดรคาร์บอน
TH35830B (th) การดำเนินกระบวนการก๊าซไฮโดรคาร์บอน
TH109436A (th) กระบวนการของก๊าซธรรมชาติเหลวและก๊าซไฮโดรคาร์บอน
TH60953B (th) กระบวนการของก๊าซธรรมชาติเหลวและก๊าซไฮโดรคาร์บอน
TW201722530A (zh) 藉由分離技術處理含有烴類及硫化合物的物質混合物之方法及系統
TH55215B (th) กระบวนการของก๊าซธรรมชาติเหลวและก๊าซไฮโดรคาร์บอน
TH117464A (th) กระบวนการของก๊าซธรรมชาติเหลวและก๊าซไฮโดรคาร์บอน

Legal Events

Date Code Title Description
FG Grant, registration