MY161644A - Process for liquefying a hydrocarbon-rich fraction - Google Patents

Process for liquefying a hydrocarbon-rich fraction

Info

Publication number
MY161644A
MY161644A MYPI2011004663A MYPI2011004663A MY161644A MY 161644 A MY161644 A MY 161644A MY PI2011004663 A MYPI2011004663 A MY PI2011004663A MY PI2011004663 A MYPI2011004663 A MY PI2011004663A MY 161644 A MY161644 A MY 161644A
Authority
MY
Malaysia
Prior art keywords
hydrocarbon
fraction
cooled
temperature level
rich fraction
Prior art date
Application number
MYPI2011004663A
Inventor
Heinz Bauer
Daniel Garthe
Original Assignee
Linde Ag
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 Linde Ag filed Critical Linde Ag
Publication of MY161644A publication Critical patent/MY161644A/en

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/003Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production
    • F25J1/0047Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle
    • F25J1/0052Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle by vaporising a liquid refrigerant stream
    • F25J1/0055Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle by vaporising a liquid refrigerant stream originating from an incorporated cascade
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/0002Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
    • F25J1/0022Hydrocarbons, e.g. natural gas
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0211Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using a multi-component refrigerant [MCR] fluid in a closed vapor compression cycle
    • F25J1/0212Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using a multi-component refrigerant [MCR] fluid in a closed vapor compression cycle as a single flow MCR cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2245/00Processes or apparatus involving steps for recycling of process streams
    • F25J2245/02Recycle of a stream in general, e.g. a by-pass stream

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (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)

Abstract

A PROCESS IS DESCRIBED FOR LIQUEFYING A HYDROCARBON-RICH FRACTION, WHEREIN THE HYDROCARBON-RICH FRACTION IS COOLED AND LIQUEFIED IN INDIRECT HEAT EXCHANGE AGAINST THE MIXED REFRIGERANT OF A MIXED REFRIGERANT CYCLE, THE MIXED REFRIGERANT IS COMPRESSED IN AT LEAST TWO STAGES AND AFTER EACH COMPRESSION STAGE IS SEPARATED INTO A GASEOUS FRACTION AND A LIQUID FRACTION, WHEREIN THE GASEOUS FRACTION OF THE LAST COMPRESSION STAGE IS COOLED TO THE LOWEST TEMPERATURE LEVEL, WHILE THE LIQUID FRACTION OF THE INTERMEDIATE COMPRESSION STAGES, OR AT LEAST ONE OF THE INTERMEDIATE COMPRESSION STAGES, IS COOLED TO A TEMPERATURE LEVEL ABOVE THE LOWEST TEMPERATURE LEVEL. ACCORDING TO THE INVENTION, THE LIQUID FRACTION (3) WHICH IS COOLED TO A TEMPERATURE LEVEL ABOVE THE LOWEST TEMPERATURE LEVEL IS COOLED (E3) UPSTREAM OF THE INDIRECT HEAT EXCHANGE (E) WITH THE HYDROCARBON-RICH FRACTION (20) WHICH IS TO BE LIQUEFIED.
MYPI2011004663A 2009-04-02 2010-03-30 Process for liquefying a hydrocarbon-rich fraction MY161644A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE102009016046A DE102009016046A1 (en) 2009-04-02 2009-04-02 Process for liquefying a hydrocarbon-rich fraction

Publications (1)

Publication Number Publication Date
MY161644A true MY161644A (en) 2017-04-28

Family

ID=42675003

Family Applications (1)

Application Number Title Priority Date Filing Date
MYPI2011004663A MY161644A (en) 2009-04-02 2010-03-30 Process for liquefying a hydrocarbon-rich fraction

Country Status (11)

Country Link
CN (1) CN102575896B (en)
AR (1) AR076136A1 (en)
AU (1) AU2010230576B2 (en)
BR (1) BRPI1013386A2 (en)
CL (1) CL2011002391A1 (en)
DE (1) DE102009016046A1 (en)
MY (1) MY161644A (en)
NO (1) NO20111413A1 (en)
PE (1) PE20120848A1 (en)
RU (1) RU2538156C2 (en)
WO (1) WO2010112206A2 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102011010633A1 (en) * 2011-02-08 2012-08-09 Linde Ag Method for cooling a one-component or multi-component stream
DE102014018412A1 (en) * 2014-12-09 2016-06-09 Linde Aktiengesellschaft Flare-free starting of a natural gas liquefaction process
DE102015004125A1 (en) * 2015-03-31 2016-10-06 Linde Aktiengesellschaft Process for liquefying a hydrocarbon-rich fraction
US10323880B2 (en) 2016-09-27 2019-06-18 Air Products And Chemicals, Inc. Mixed refrigerant cooling process and system
US10852059B2 (en) 2017-09-28 2020-12-01 Air Products And Chemicals, Inc. Multiple pressure mixed refrigerant cooling system
US10753676B2 (en) 2017-09-28 2020-08-25 Air Products And Chemicals, Inc. Multiple pressure mixed refrigerant cooling process

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4325231A (en) * 1976-06-23 1982-04-20 Heinrich Krieger Cascade cooling arrangement
FR2540612A1 (en) * 1983-02-08 1984-08-10 Air Liquide METHOD AND INSTALLATION FOR COOLING A FLUID, IN PARTICULAR A LIQUEFACTION OF NATURAL GAS
US4525185A (en) * 1983-10-25 1985-06-25 Air Products And Chemicals, Inc. Dual mixed refrigerant natural gas liquefaction with staged compression
DE19722490C1 (en) * 1997-05-28 1998-07-02 Linde Ag Single flow liquefaction of hydrocarbon-rich stream especially natural gas with reduced energy consumption
GB2326464B (en) * 1997-06-12 2001-06-06 Costain Oil Gas & Process Ltd Refrigeration cycle using a mixed refrigerant
GB9712304D0 (en) * 1997-06-12 1997-08-13 Costain Oil Gas & Process Limi Refrigeration cycle using a mixed refrigerant
US6347531B1 (en) * 1999-10-12 2002-02-19 Air Products And Chemicals, Inc. Single mixed refrigerant gas liquefaction process
US6347532B1 (en) * 1999-10-12 2002-02-19 Air Products And Chemicals, Inc. Gas liquefaction process with partial condensation of mixed refrigerant at intermediate temperatures
US6742357B1 (en) * 2003-03-18 2004-06-01 Air Products And Chemicals, Inc. Integrated multiple-loop refrigeration process for gas liquefaction
EP1864064A1 (en) * 2005-03-09 2007-12-12 Shell Internationale Research Maatschappij B.V. Method for the liquefaction of a hydrocarbon-rich system
CN201417042Y (en) * 2009-04-27 2010-03-03 赵德泉 Equipment with simplified mixed refrigerant liquefaction process

Also Published As

Publication number Publication date
RU2011144360A (en) 2013-05-10
AU2010230576B2 (en) 2016-02-18
WO2010112206A3 (en) 2012-10-11
BRPI1013386A2 (en) 2016-03-29
AR076136A1 (en) 2011-05-18
DE102009016046A1 (en) 2010-10-07
CL2011002391A1 (en) 2012-02-10
AU2010230576A1 (en) 2011-09-15
NO20111413A1 (en) 2011-10-18
CN102575896A (en) 2012-07-11
WO2010112206A2 (en) 2010-10-07
RU2538156C2 (en) 2015-01-10
CN102575896B (en) 2015-04-22
PE20120848A1 (en) 2012-07-11

Similar Documents

Publication Publication Date Title
MY165162A (en) Multi nitrogen expansion process for lng production
MY174487A (en) Integrated pre-cooled mixed refrigerant system and method
MY161644A (en) Process for liquefying a hydrocarbon-rich fraction
WO2009130466A3 (en) Dual nitrogen expansion process
WO2014013158A3 (en) Method for liquefying a natural gas, including a phase change
RU2009100154A (en) METHOD FOR LIQUID HYDROGEN
WO2010128467A3 (en) Production and distribution of natural gas
GB2479940B (en) Process and apparatus for the liquefaction of natural gas
WO2012175889A3 (en) Method for liquefying natural gas with a triple closed circuit of coolant gas
WO2012172281A4 (en) Process for liquefaction of natural gas
WO2008022689A3 (en) Method for the liquefaction of a hydrocarbon-rich flow
MY180003A (en) Method of cooling using extended binary refrigeration system
ATE499567T1 (en) SYSTEM FOR COLD COMPRESSION OF AN AIR STREAM WITH COOLING BY NATURAL GAS
WO2012175887A3 (en) Method for liquefying natural gas with a mixture of coolant gas
WO2010121752A3 (en) Method for liquefying a hydrocarbon-rich fraction
WO2011136543A3 (en) Natural gas liquefaction process
WO2012023752A3 (en) Natural gas liquefaction process
WO2012057505A3 (en) Natural gas liquefaction process
CL2011001938A1 (en) Process to liquefy a fraction rich in hydrocarbon with removal of a fraction rich in c2 +, with heat exchange with mixed refrigerant, which is separated into a gaseous and liquid fraction, where occasionally a refrigerant undercurrent is expanded and added to the liquid fraction mixed refrigerant.
WO2009057179A3 (en) Small-scale plant for production of liquified natural gas
WO2012140369A3 (en) Method and apparatus for liquefying a gas or cooling a feed gas at supercritical pressure
WO2008095713A3 (en) Method for liquefying a stream rich in hydrocarbons
WO2011114012A3 (en) Process for liquefying a natural gas with refrigerant mixtures containing at least one unsaturated hydrocarbon
TH136309B (en) Process for liquefying hydrocarbon-rich portions
TH118028B (en) Method for liquefying hydrocarbon-rich portions