PE20121168A1 - PROCESSING OF HYDROCARBON GASES - Google Patents

PROCESSING OF HYDROCARBON GASES

Info

Publication number
PE20121168A1
PE20121168A1 PE2011002068A PE2011002068A PE20121168A1 PE 20121168 A1 PE20121168 A1 PE 20121168A1 PE 2011002068 A PE2011002068 A PE 2011002068A PE 2011002068 A PE2011002068 A PE 2011002068A PE 20121168 A1 PE20121168 A1 PE 20121168A1
Authority
PE
Peru
Prior art keywords
current
supplied
vapor
distillation
absorption
Prior art date
Application number
PE2011002068A
Other languages
Spanish (es)
Inventor
Andrew F Johnke
John D Wilkinson
Joe T Lynch
Hank M Hudson
Kyle T Cuellar
Larry W Lewis
Original Assignee
Ortloff Engineers Ltd
Sme Products Lp
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
Priority claimed from US12/689,616 external-priority patent/US9021831B2/en
Application filed by Ortloff Engineers Ltd, Sme Products Lp filed Critical Ortloff Engineers Ltd
Publication of PE20121168A1 publication Critical patent/PE20121168A1/en

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
    • 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • 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
    • 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
    • C10G5/06—Recovery of liquid hydrocarbon mixtures from gases, e.g. natural gas by cooling or compressing
    • 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
    • F25J5/00—Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants
    • 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
    • F25J2200/70—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
    • 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
    • F25J2210/06—Splitting of the feed stream, e.g. for treating or cooling in different ways
    • 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
    • F25J2270/00—Refrigeration techniques used
    • F25J2270/12—External refrigeration with liquid vaporising loop
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2270/00—Refrigeration techniques used
    • F25J2270/60—Closed external refrigeration cycle with single component refrigerant [SCR], e.g. C1-, C2- or C3-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
    • 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.
    • 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
    • F25J2290/42—Modularity, pre-fabrication of modules, assembling and erection, horizontal layout, i.e. plot plan, and vertical arrangement of parts of the cryogenic unit, e.g. of the cold box

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • Separation By Low-Temperature Treatments (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

REFERIDO A UN PROCESO Y APARATO PARA LA RECUPERACION DE ETANO, ETILENO, PROPANO, PROPILENO Y COMPONENTES DE HIDROCARBUROS MAS PESADOS DE UNA CORRIENTE DE GAS DE HIDROCARBUROS EN UN CONJUNTO DE TRATAMIENTO COMPACTO. LA CORRIENTE DE GAS SE ENFRIA Y SE DIVIDE EN UNA PRIMERA Y UNA SEGUNDA CORRIENTE. LA PRIMERA CORRIENTE SE ENFRIA ADICIONALMENTE PARA CONDENSARLA SUSTANCIALMENTE POR COMPLETO, Y LUEGO SE LA EXPANDE A UNA PRESION MENOR Y SE LA SUMINISTRA COMO ALIMENTACION ENTRE EL PRIMERO Y EL SEGUNDO MEDIOS DE ABSORCION DENTRO DEL CONJUNTO DE TRATAMIENTO. LA SEGUNDA CORRIENTE SE EXPANDE A UNA PRESION MENOR Y SE LA SUMINISTRA COMO UNA ALIMENTACION DEL FONDO AL SEGUNDO MEDIO DE ABSORCION. SE RECOLECTA UNA CORRIENTE DE VAPOR DE DESTILACION DE LA REGION SUPERIOR DEL PRIMER MEDIO ABSORBENTE Y SE LA DIRIGE A UNO O MAS MEDIOS INTERCAMBIADORES DE CALOR EN EL CONJUNTO DE TRATAMIENTO PARA CALENTARLA, AL TIEMPO QUE SE ENFRIA LA CORRIENTE DE GAS Y LA PRIMERA CORRIENTE. LA CORRIENTE DE VAPOR PARA LA DESTILACION CALIENTE SE COMPRIME A UNA PRESION MAYOR Y SE DIVIDE EN UNA FRACCION DE GAS RESIDUAL VOLATIL Y UNA CORRIENTE DE RECICLAJE COMPRIMIDA. LA CORRIENTE DE RECICLAJE COMPRIMIDA SE ENFRIA HASTA CONDENSARLA SUSTANCIALMENTE POR COMPLETO MEDIANTE LA CORRIENTE DE VAPOR PARA LA DESTILACION EN LOS UNO O MAS MEDIOS DE INTERCAMBIO DE CALOR DENTRO DEL CONJUNTO DE TRATAMIENTO, Y LUEGO, SE LA EXPANDE A UNA PRESION MENOR Y SE LA SUMINISTRA COMO ALIMENTACION SUPERIOR AL PRIMER MEDIO DE ABSORCIONREFERRED TO A PROCESS AND APPARATUS FOR THE RECOVERY OF ETHANE, ETHYLENE, PROPANE, PROPYLENE AND HEAVY-DUTY HYDROCARBON COMPONENTS FROM A HYDROCARBON GAS FLOW IN A COMPACT TREATMENT SET. THE GAS CURRENT COOLS AND DIVIDES INTO A FIRST AND A SECOND CURRENT. THE FIRST CURRENT IS ADDITIONALLY COOLED TO SUBSTANTIALLY CONDENSING IT COMPLETELY, AND THEN IS EXPANDED TO A LOWER PRESSURE AND SUPPLIED AS A FEED BETWEEN THE FIRST AND SECOND ABSORPTION MEANS WITHIN THE TREATMENT SET. THE SECOND CURRENT IS EXPANDED AT A LOWER PRESSURE AND IS SUPPLIED AS A FEED FROM THE BOTTOM TO THE SECOND ABSORPTION MEDIUM. A STREAM OF DISTILLATION VAPOR IS COLLECTED FROM THE UPPER REGION OF THE FIRST ABSORBING MEDIA AND DIRECTED TO ONE OR MORE HEAT EXCHANGING MEDIA IN THE TREATMENT ASSEMBLY TO HEAT IT, AS THE GAS STREAM AND FIRST CURRENT COOL. THE VAPOR CURRENT FOR HOT DISTILLATION IS COMPRESSED AT A HIGHER PRESSURE AND DIVIDES INTO A VOLATILE RESIDUAL GAS FRACTION AND A COMPRESSED RECYCLING CURRENT. THE COMPRESSED RECYCLING CURRENT IS COOLED UNTIL SUBSTANTIALLY COMPLETELY CONDENSED BY THE VAPOR CURRENT FOR DISTILLATION IN THE ONE OR MORE HEAT EXCHANGE MEDIA WITHIN THE TREATMENT ASSEMBLY, AND THEN, IS SUPPLIED TO PRESSURE AS FEEDING SUPERIOR TO THE FIRST MEANS OF ABSORPTION

PE2011002068A 2009-06-11 2010-03-04 PROCESSING OF HYDROCARBON GASES PE20121168A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US18636109P 2009-06-11 2009-06-11
US12/689,616 US9021831B2 (en) 2009-02-17 2010-01-19 Hydrocarbon gas processing

Publications (1)

Publication Number Publication Date
PE20121168A1 true PE20121168A1 (en) 2012-08-30

Family

ID=43309149

Family Applications (1)

Application Number Title Priority Date Filing Date
PE2011002068A PE20121168A1 (en) 2009-06-11 2010-03-04 PROCESSING OF HYDROCARBON GASES

Country Status (13)

Country Link
EP (1) EP2440311A1 (en)
JP (1) JP5552159B2 (en)
KR (1) KR101643796B1 (en)
CN (1) CN102596361B (en)
AU (1) AU2010259236B2 (en)
CA (1) CA2763698C (en)
CO (1) CO6480938A2 (en)
EA (1) EA022763B1 (en)
MX (1) MX2011013079A (en)
MY (1) MY162763A (en)
PE (1) PE20121168A1 (en)
TN (1) TN2011000624A1 (en)
WO (1) WO2010144163A1 (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BRPI1105771A2 (en) * 2010-03-31 2016-05-03 Orlloff Engineers Ltd hydrocarbon gas processing.
CN104069717A (en) * 2013-03-29 2014-10-01 张家港市苏承环保设备有限公司 Solvent separating and processing device
CN105531552B (en) * 2013-09-11 2018-05-25 奥特洛夫工程有限公司 Hydrocarbon gas processing
KR102099798B1 (en) * 2013-09-11 2020-04-13 유오피 엘엘씨 Hydrocarbon gas processing
CN104792116B (en) * 2014-11-25 2017-08-08 中国寰球工程公司 A kind of natural gas reclaims the system and technique of ethane and ethane above lighter hydrocarbons
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
CN108507277A (en) * 2018-04-28 2018-09-07 中国石油工程建设有限公司 A kind of the cold comprehensive utilization device and method of natural gas ethane recovery
US10982898B2 (en) 2018-05-11 2021-04-20 Air Products And Chemicals, Inc. Modularized LNG separation device and flash gas heat exchanger

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JPS546500B1 (en) * 1976-02-15 1979-03-29
US5568737A (en) * 1994-11-10 1996-10-29 Elcor Corporation Hydrocarbon gas processing
UA76750C2 (en) * 2001-06-08 2006-09-15 Елккорп Method for liquefying natural gas (versions)
US6742358B2 (en) * 2001-06-08 2004-06-01 Elkcorp Natural gas liquefaction
US7484385B2 (en) * 2003-01-16 2009-02-03 Lummus Technology Inc. Multiple reflux stream hydrocarbon recovery process
BRPI0407806A (en) * 2003-02-25 2006-02-14 Ortloff Engineers Ltd hydrocarbon gas processing
WO2005114076A1 (en) * 2004-04-26 2005-12-01 Ortloff Engineers, Ltd Natural gas liquefaction
US8590340B2 (en) * 2007-02-09 2013-11-26 Ortoff Engineers, Ltd. Hydrocarbon gas processing

Also Published As

Publication number Publication date
MX2011013079A (en) 2012-02-01
CN102596361B (en) 2015-06-03
JP5552159B2 (en) 2014-07-16
CN102596361A (en) 2012-07-18
WO2010144163A8 (en) 2012-04-19
EA022763B1 (en) 2016-02-29
CO6480938A2 (en) 2012-07-16
KR101643796B1 (en) 2016-07-29
AU2010259236A8 (en) 2012-09-06
MY162763A (en) 2017-07-14
WO2010144163A1 (en) 2010-12-16
EP2440311A1 (en) 2012-04-18
JP2012529620A (en) 2012-11-22
KR20120026607A (en) 2012-03-19
TN2011000624A1 (en) 2013-05-24
EA201270002A1 (en) 2012-07-30
AU2010259236A1 (en) 2012-02-23
CA2763698A1 (en) 2010-12-16
CA2763698C (en) 2016-08-16
AU2010259236B2 (en) 2015-11-05
AU2010259236A2 (en) 2012-06-07

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