MY161644A - Process for liquefying a hydrocarbon-rich fraction - Google Patents
Process for liquefying a hydrocarbon-rich fractionInfo
- 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
Links
- 238000000034 method Methods 0.000 title abstract 2
- 239000004215 Carbon black (E152) Substances 0.000 title 1
- 229930195733 hydrocarbon Natural products 0.000 title 1
- 150000002430 hydrocarbons Chemical class 0.000 title 1
- 230000006835 compression Effects 0.000 abstract 4
- 238000007906 compression Methods 0.000 abstract 4
- 239000007788 liquid Substances 0.000 abstract 3
- 239000003507 refrigerant Substances 0.000 abstract 3
- 238000011144 upstream manufacturing Methods 0.000 abstract 1
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
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/003—Processes 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
- F25J1/0047—Processes 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
- F25J1/0052—Processes 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
- F25J1/0055—Processes 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
-
- 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
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/0002—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
- F25J1/0022—Hydrocarbons, e.g. 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
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/02—Processes 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
- F25J1/0211—Processes 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
- F25J1/0212—Processes 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
-
- 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
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.
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)
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)
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 |
-
2009
- 2009-04-02 DE DE102009016046A patent/DE102009016046A1/en not_active Withdrawn
-
2010
- 2010-03-18 AR ARP100100874A patent/AR076136A1/en not_active Application Discontinuation
- 2010-03-30 MY MYPI2011004663A patent/MY161644A/en unknown
- 2010-03-30 WO PCT/EP2010/002034 patent/WO2010112206A2/en active Application Filing
- 2010-03-30 CN CN201080015211.2A patent/CN102575896B/en not_active Expired - Fee Related
- 2010-03-30 BR BRPI1013386A patent/BRPI1013386A2/en not_active Application Discontinuation
- 2010-03-30 AU AU2010230576A patent/AU2010230576B2/en not_active Ceased
- 2010-03-30 RU RU2011144360/06A patent/RU2538156C2/en not_active IP Right Cessation
- 2010-03-30 PE PE2011001669A patent/PE20120848A1/en not_active Application Discontinuation
-
2011
- 2011-09-27 CL CL2011002391A patent/CL2011002391A1/en unknown
- 2011-10-18 NO NO20111413A patent/NO20111413A1/en not_active Application Discontinuation
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 |
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