PE20120675A1 - PROCESS FOR THE LIQUEFACTION OF A CURRENT RICH IN HYDROCARBONS - Google Patents
PROCESS FOR THE LIQUEFACTION OF A CURRENT RICH IN HYDROCARBONSInfo
- Publication number
- PE20120675A1 PE20120675A1 PE2011001423A PE2011001423A PE20120675A1 PE 20120675 A1 PE20120675 A1 PE 20120675A1 PE 2011001423 A PE2011001423 A PE 2011001423A PE 2011001423 A PE2011001423 A PE 2011001423A PE 20120675 A1 PE20120675 A1 PE 20120675A1
- Authority
- PE
- Peru
- Prior art keywords
- fraction
- mixed refrigerant
- rich
- liquefaction
- expanded
- Prior art date
Links
- 229930195733 hydrocarbon Natural products 0.000 title abstract 3
- 150000002430 hydrocarbons Chemical class 0.000 title abstract 3
- 238000000034 method Methods 0.000 title abstract 2
- 239000003507 refrigerant Substances 0.000 abstract 5
- 239000007788 liquid Substances 0.000 abstract 2
- 239000004215 Carbon black (E152) Substances 0.000 abstract 1
- 238000000605 extraction 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
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B9/00—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
- F25B9/002—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant
- F25B9/006—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant the refrigerant containing more than one component
-
- 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
- F25J1/003—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
- F25J1/02—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
- 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
- F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
- F25J1/0244—Operation; Control and regulation; Instrumentation
-
- 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
- F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
- F25J1/0279—Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc.
- F25J1/0291—Refrigerant compression by combined gas compression and liquid pumping
-
- 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
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B1/00—Compression machines, plants or systems with non-reversible cycle
- F25B1/10—Compression machines, plants or systems with non-reversible cycle with multi-stage compression
-
- 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
- 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
- F25J2215/00—Processes characterised by the type or other details of the product stream
- F25J2215/04—Recovery of liquid products
-
- 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
- F25J2270/00—Refrigeration techniques used
- F25J2270/18—External refrigeration with incorporated cascade 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
- F25J2270/66—Closed external refrigeration cycle with multi component refrigerant [MCR], e.g. 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
- F25J2270/00—Refrigeration techniques used
- F25J2270/90—External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration
- F25J2270/902—Details about the refrigeration cycle used, e.g. composition of refrigerant, arrangement of compressors or cascade, make up sources, use of reflux 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
- F25J2280/00—Control of the process or apparatus
- F25J2280/02—Control in general, load changes, different modes ("runs"), measurements
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)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
REFERIDO A UN PROCESO PARA LA LICUEFACCION DE UNA CORRIENTE RICA EN HIDROCARBUROS CON LA EXTRACCION SIMULTANEA DE UNA FRACCION RICA EN C2, EN EL CUAL EL ENFRIAMIENTO Y LICUEFACCION DE LA FRACCION RICA EN HIDROCARBUROS TIENEN LUGAR EN UN INTERCAMBIO DE CALOR INDIRECTO CON EL REFRIGERANTE MIXTO DE UN CICLO DE REFRIGERANTE MIXTO EN EL CUAL EL REFRIGERANTE MIXTO ES COMPRIMIDO EN POR LO MENOS DOS ETAPAS, Y LA FRACCION RICA EN C2 ES EXTRAIDA EN UN NIVEL DE TEMPERATURA AJUSTABLE, EN EL CUAL EL REFRIGERANTE MIXTO ES SEPARADO EN UNA FRACCION GASEOSA Y UNA FRACCION LIQUIDA, AMBAS FRACCIONES SON SUBENFRIADAS, EXPANDIDAS ESENCIALMENTE A PRESION DE SUCCION DE LA PRIMERA ETAPA DEL COMPRESOR Y, AL MENOS EN PARTE, VAPORIZADAS. AL MENOS UNA SUBCORRIENTE DE LA FRACCION LICUADA ANTERIORMENTE GASEOSA DEL REFRIGERANTE MIXTO ES EXPANDIDA Y AGREGADA A LA FRACCION LQUIDA EXPANDIDA DEL REFRIGERANTE MIXTOREFERRED TO A PROCESS FOR THE LIQUEFACTION OF A CURRENT RICH IN HYDROCARBONS WITH THE SIMULTANEOUS EXTRACTION OF A FRACTION RICH IN C2, IN WHICH THE COOLING AND LIQUEFACTION OF THE RICH FRACTION IN HYDROCARBON TAKES PLACE OF A HEAT REFURBISHED INTERCHANGE A MIXED REFRIGERANT CYCLE IN WHICH THE MIXED REFRIGERANT IS COMPRESSED IN AT LEAST TWO STAGES, AND THE C2-RICH FRACTION IS EXTRACTED AT AN ADJUSTABLE TEMPERATURE LEVEL, IN WHICH THE MIXED REFRIGERANT IS SEPARATED IN A FRACTIONAL FRACTION. LIQUID, BOTH FRACTIONS ARE SUBCOOLED, ESSENTIALLY EXPANDED UNDER SUCTION PRESSURE OF THE COMPRESSOR FIRST STAGE AND, AT LEAST IN PART, VAPORIZED. AT LEAST A SUB-CURRENT OF THE PREVIOUSLY GASEOUS LIQUEFIED FRACTION OF THE MIXED REFRIGERANT IS EXPANDED AND ADDED TO THE EXPANDED LIQUID FRACTION OF THE MIXED REFRIGERANT
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102009008230A DE102009008230A1 (en) | 2009-02-10 | 2009-02-10 | Process for liquefying a hydrocarbon-rich stream |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| PE20120675A1 true PE20120675A1 (en) | 2012-06-03 |
Family
ID=42317492
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PE2011001423A PE20120675A1 (en) | 2009-02-10 | 2010-02-02 | PROCESS FOR THE LIQUEFACTION OF A CURRENT RICH IN HYDROCARBONS |
Country Status (11)
| Country | Link |
|---|---|
| CN (1) | CN102449419B (en) |
| AR (1) | AR075133A1 (en) |
| AU (1) | AU2010213188B2 (en) |
| BR (1) | BRPI1008539B1 (en) |
| CL (1) | CL2011001938A1 (en) |
| DE (1) | DE102009008230A1 (en) |
| MY (1) | MY159967A (en) |
| NO (1) | NO20111214A1 (en) |
| PE (1) | PE20120675A1 (en) |
| RU (1) | RU2537480C2 (en) |
| WO (1) | WO2010091804A2 (en) |
Families Citing this family (7)
| 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 |
| DE102012021637A1 (en) * | 2012-11-02 | 2014-05-08 | Linde Aktiengesellschaft | Process for cooling a hydrocarbon-rich fraction |
| DE102013016695A1 (en) * | 2013-10-08 | 2015-04-09 | Linde Aktiengesellschaft | Process for liquefying a hydrocarbon-rich fraction |
| DE102014005936A1 (en) * | 2014-04-24 | 2015-10-29 | Linde Aktiengesellschaft | Process for liquefying a hydrocarbon-rich fraction |
| US20160109177A1 (en) | 2014-10-16 | 2016-04-21 | General Electric Company | System and method for natural gas liquefaction |
| DE102015002443A1 (en) * | 2015-02-26 | 2016-09-01 | Linde Aktiengesellschaft | Process for liquefying natural gas |
| DE102015004125A1 (en) * | 2015-03-31 | 2016-10-06 | Linde Aktiengesellschaft | Process for liquefying a hydrocarbon-rich fraction |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1619728C3 (en) * | 1967-12-21 | 1974-02-07 | Linde Ag, 6200 Wiesbaden | Low-temperature rectification process for separating gas mixtures from components whose boiling temperatures are far apart |
| DE3531307A1 (en) * | 1985-09-02 | 1987-03-05 | Linde Ag | METHOD FOR SEPARATING C (ARROW DOWN) 2 (ARROW DOWN) (ARROW DOWN) + (ARROW DOWN) HYDROCARBONS FROM NATURAL GAS |
| DE19722490C1 (en) | 1997-05-28 | 1998-07-02 | Linde Ag | Single flow liquefaction of hydrocarbon-rich stream especially natural gas with reduced energy consumption |
| US5983665A (en) * | 1998-03-03 | 1999-11-16 | Air Products And Chemicals, Inc. | Production of refrigerated liquid methane |
| US6158240A (en) * | 1998-10-23 | 2000-12-12 | Phillips Petroleum Company | Conversion of normally gaseous material to liquefied product |
| US6401486B1 (en) * | 2000-05-18 | 2002-06-11 | Rong-Jwyn Lee | Enhanced NGL recovery utilizing refrigeration and reflux from LNG plants |
| US7082787B2 (en) * | 2004-03-09 | 2006-08-01 | Bp Corporation North America Inc. | Refrigeration system |
| RU2297580C1 (en) * | 2005-08-23 | 2007-04-20 | Михаил Васильевич Кнатько | Method of liquefying natural gas |
-
2009
- 2009-02-10 DE DE102009008230A patent/DE102009008230A1/en not_active Withdrawn
-
2010
- 2010-01-12 AR ARP100100071A patent/AR075133A1/en active IP Right Grant
- 2010-02-02 RU RU2011137411/06A patent/RU2537480C2/en active
- 2010-02-02 AU AU2010213188A patent/AU2010213188B2/en active Active
- 2010-02-02 BR BRPI1008539-4A patent/BRPI1008539B1/en not_active IP Right Cessation
- 2010-02-02 PE PE2011001423A patent/PE20120675A1/en active IP Right Grant
- 2010-02-02 CN CN201080007356.8A patent/CN102449419B/en not_active Expired - Fee Related
- 2010-02-02 MY MYPI2011003699A patent/MY159967A/en unknown
- 2010-02-02 WO PCT/EP2010/000614 patent/WO2010091804A2/en not_active Ceased
-
2011
- 2011-08-10 CL CL2011001938A patent/CL2011001938A1/en unknown
- 2011-09-08 NO NO20111214A patent/NO20111214A1/en not_active Application Discontinuation
Also Published As
| Publication number | Publication date |
|---|---|
| BRPI1008539B1 (en) | 2020-08-04 |
| AU2010213188B2 (en) | 2015-12-24 |
| RU2011137411A (en) | 2013-03-20 |
| BRPI1008539A2 (en) | 2016-03-15 |
| RU2537480C2 (en) | 2015-01-10 |
| CN102449419B (en) | 2015-10-07 |
| AU2010213188A1 (en) | 2011-08-18 |
| AR075133A1 (en) | 2011-03-09 |
| CL2011001938A1 (en) | 2011-10-28 |
| CN102449419A (en) | 2012-05-09 |
| WO2010091804A2 (en) | 2010-08-19 |
| MY159967A (en) | 2017-02-15 |
| NO20111214A1 (en) | 2011-09-08 |
| DE102009008230A1 (en) | 2010-08-12 |
| WO2010091804A3 (en) | 2012-09-20 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| PE20120675A1 (en) | PROCESS FOR THE LIQUEFACTION OF A CURRENT RICH IN HYDROCARBONS | |
| RU2016130315A (en) | SYSTEM AND METHOD FOR LIQUIDING NATURAL GAS | |
| US8635885B2 (en) | Configurations and methods of heating value control in LNG liquefaction plant | |
| PE20130936A1 (en) | SYSTEM AND METHOD FOR INTEGRATED PRE-COOLING OF MIXED REFRIGERANT | |
| CO2018013887A2 (en) | Process for liquefying natural gas and for recovering possible liquids from natural gas, which comprise two semi-open refrigerant cycles for natural gas and a closed refrigerant cycle for refrigerant gas | |
| EA200800267A1 (en) | INSTALLATIONS AND METHODS OF COMBINED EXTRACTION OF NATURAL GAS CONDENSATE AND LIQUIDATION OF LIQUEFIED NATURAL GAS | |
| EP3118548A3 (en) | Integrated methane refrigeration system for liquefying natural gas | |
| AR083476A1 (en) | SIMPLIFIED PROCEDURE FOR THE PRODUCTION OF A CURRENT ENERGY IN METHANE AND A COURT RICH IN HYDROCARBONS IN CA FROM A NATURAL LOAD GAS CURRENT, AND ASSOCIATED INSTALLATION | |
| AR087469A1 (en) | PROCESS AND INSTALLATION FOR NATURAL GAS LICUEFACTION | |
| GB201007297D0 (en) | Process and apparatus for the liquefaction of natural gas | |
| MX2014014750A (en) | SYSTEM AND METHOD FOR THE LIQUORATION OF NATURAL GAS. | |
| RU2015135574A (en) | PRODUCTION OF LIQUEFIED NATURAL GAS | |
| MX2017010541A (en) | Method and apparatus for obtaining a compressed nitrogen product. | |
| PE20121108A1 (en) | METHOD FOR THE LIQUEFACTION OF A FRACTION RICH IN HYDROCARBONS | |
| MY178765A (en) | Method and apparatus for producing a liquefied hydrocarbon stream | |
| PE20120848A1 (en) | PROCESS FOR LIQUEFACTION OF A FRACTION RICH IN HYDROCARBONS | |
| RU2016105466A (en) | NATURAL GAS LIQUID METHOD | |
| CL2008000382A1 (en) | Process to liquefy hydrocarbon-rich flow in a closed circuit consisting of three refrigerants, where the refrigerant mixture of each circuit is vaporized at a pressure level and the heat exchange between the hydrocarbon-rich flow and the pre-cooling mixture is carried out in two or more exchangers in parallel. | |
| AR091267A1 (en) | PROCEDURE FOR LIQUIDING A FRACTION RICH IN HYDROCARBONS | |
| AR067129A1 (en) | PROCEDURE TO COOL OR LIQUIDIFY A CURRENT RICH IN HYDROCARBONS | |
| RU2014108021A (en) | NATURAL GAS LIQUID METHOD | |
| MY172908A (en) | Method and apparatus for producing a liquefied hydrocarbon stream | |
| WO2007020252A3 (en) | Method and arrangement for liquefying a stream rich in hydrocarbons | |
| CA2755079C (en) | Configurations and methods of heating value control in lng liquefaction plant | |
| TH136309A (en) | Process for liquefying hydrocarbon-rich portions |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FG | Grant, registration |