DE102009008230A1 - Verfahren zum Verflüssigen eines Kohlenwasserstoff-reichen Stromes - Google Patents
Verfahren zum Verflüssigen eines Kohlenwasserstoff-reichen Stromes Download PDFInfo
- Publication number
- DE102009008230A1 DE102009008230A1 DE102009008230A DE102009008230A DE102009008230A1 DE 102009008230 A1 DE102009008230 A1 DE 102009008230A1 DE 102009008230 A DE102009008230 A DE 102009008230A DE 102009008230 A DE102009008230 A DE 102009008230A DE 102009008230 A1 DE102009008230 A1 DE 102009008230A1
- Authority
- DE
- Germany
- Prior art keywords
- fraction
- refrigerant mixture
- rich fraction
- hydrocarbon
- liquefied
- Prior art date
- Legal status (The legal status 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 status listed.)
- Withdrawn
Links
- 229930195733 hydrocarbon Natural products 0.000 title claims abstract description 32
- 150000002430 hydrocarbons Chemical class 0.000 title claims abstract description 32
- 238000000034 method Methods 0.000 title claims abstract description 30
- 239000004215 Carbon black (E152) Substances 0.000 title claims abstract description 27
- 239000003507 refrigerant Substances 0.000 claims abstract description 53
- 239000000203 mixture Substances 0.000 claims abstract description 45
- 238000000926 separation method Methods 0.000 claims abstract description 36
- 239000007788 liquid Substances 0.000 claims abstract description 21
- 238000001816 cooling Methods 0.000 claims abstract description 3
- 238000009835 boiling Methods 0.000 claims description 3
- 238000004781 supercooling Methods 0.000 claims description 3
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 22
- 239000003949 liquefied natural gas Substances 0.000 description 11
- 239000003345 natural gas Substances 0.000 description 9
- 238000001704 evaporation Methods 0.000 description 4
- 230000008020 evaporation Effects 0.000 description 4
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- 230000001419 dependent effect Effects 0.000 description 2
- 238000004886 process control Methods 0.000 description 2
- BUHVIAUBTBOHAG-FOYDDCNASA-N (2r,3r,4s,5r)-2-[6-[[2-(3,5-dimethoxyphenyl)-2-(2-methylphenyl)ethyl]amino]purin-9-yl]-5-(hydroxymethyl)oxolane-3,4-diol Chemical compound COC1=CC(OC)=CC(C(CNC=2C=3N=CN(C=3N=CN=2)[C@H]2[C@@H]([C@H](O)[C@@H](CO)O2)O)C=2C(=CC=CC=2)C)=C1 BUHVIAUBTBOHAG-FOYDDCNASA-N 0.000 description 1
- 206010016352 Feeling of relaxation Diseases 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 210000000540 fraction c Anatomy 0.000 description 1
- 238000012432 intermediate storage Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 239000013526 supercooled liquid Substances 0.000 description 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)
Priority Applications (11)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102009008230A DE102009008230A1 (de) | 2009-02-10 | 2009-02-10 | Verfahren zum Verflüssigen eines Kohlenwasserstoff-reichen Stromes |
ARP100100071A AR075133A1 (es) | 2009-02-10 | 2010-01-12 | Procedimiento para licuar una corriente rica en hidrocarburos |
CN201080007356.8A CN102449419B (zh) | 2009-02-10 | 2010-02-02 | 用于液化富烃流的方法 |
PCT/EP2010/000614 WO2010091804A2 (de) | 2009-02-10 | 2010-02-02 | Verfahren zum verflüssigen eines kohlenwasserstoff-reichen stromes |
BRPI1008539-4A BRPI1008539B1 (pt) | 2009-02-10 | 2010-02-02 | Processo para liquefazer uma fração rica em hidrocarbonetos |
RU2011137411/06A RU2537480C2 (ru) | 2009-02-10 | 2010-02-02 | Способ сжижения потока с высоким содержанием углеводородов |
AU2010213188A AU2010213188B2 (en) | 2009-02-10 | 2010-02-02 | Method for liquefying a hydrocarbon-rich stream |
PE2011001423A PE20120675A1 (es) | 2009-02-10 | 2010-02-02 | Proceso para la licuefaccion de una corriente rica en hidrocarburos |
MYPI2011003699A MY159967A (en) | 2009-02-10 | 2010-02-02 | Process for liquefying a hydrocarbon-rich stream |
CL2011001938A CL2011001938A1 (es) | 2009-02-10 | 2011-08-10 | Proceso para licuar una fracción rica en hidrocarbono con remoción de una fracción rica en c2+, con intercambio de calor con refrigerante mezclado, el cual es separado en una fraccion gaseosa y liquida, donde ocasionalmente una subcorriente del refrigerante es expandida y agregada a la fraccion liquida del refrigerante mezclado. |
NO20111214A NO20111214A1 (no) | 2009-02-10 | 2011-09-08 | Fremgangsmate for a gjore en hydrokarbonrik strom flytende |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102009008230A DE102009008230A1 (de) | 2009-02-10 | 2009-02-10 | Verfahren zum Verflüssigen eines Kohlenwasserstoff-reichen Stromes |
Publications (1)
Publication Number | Publication Date |
---|---|
DE102009008230A1 true DE102009008230A1 (de) | 2010-08-12 |
Family
ID=42317492
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE102009008230A Withdrawn DE102009008230A1 (de) | 2009-02-10 | 2009-02-10 | Verfahren zum Verflüssigen eines Kohlenwasserstoff-reichen Stromes |
Country Status (11)
Country | Link |
---|---|
CN (1) | CN102449419B (es) |
AR (1) | AR075133A1 (es) |
AU (1) | AU2010213188B2 (es) |
BR (1) | BRPI1008539B1 (es) |
CL (1) | CL2011001938A1 (es) |
DE (1) | DE102009008230A1 (es) |
MY (1) | MY159967A (es) |
NO (1) | NO20111214A1 (es) |
PE (1) | PE20120675A1 (es) |
RU (1) | RU2537480C2 (es) |
WO (1) | WO2010091804A2 (es) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20120198883A1 (en) * | 2011-02-08 | 2012-08-09 | Linde Aktiengesellschaft | Method for cooling a single-component or multi-component stream |
US20150096326A1 (en) * | 2013-10-08 | 2015-04-09 | Linde Aktiengesellschaft | Method for liquefying a hydrocarbon-rich fraction |
US20160109177A1 (en) * | 2014-10-16 | 2016-04-21 | General Electric Company | System and method for natural gas liquefaction |
WO2016134815A1 (de) * | 2015-02-26 | 2016-09-01 | Linde Aktiengesellschaft | Verfahren zur verflüssigen von erdgas |
DE102015004125A1 (de) * | 2015-03-31 | 2016-10-06 | Linde Aktiengesellschaft | Verfahren zum Verflüssigen einer Kohlenwasserstoff-reichen Fraktion |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102012021637A1 (de) * | 2012-11-02 | 2014-05-08 | Linde Aktiengesellschaft | Verfahren zum Abkühlen einer Kohlenwasserstoff-reichen Fraktion |
DE102014005936A1 (de) * | 2014-04-24 | 2015-10-29 | Linde Aktiengesellschaft | Verfahren zum Verflüssigen einer Kohlenwasserstoff-reichen Fraktion |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19722490C1 (de) | 1997-05-28 | 1998-07-02 | Linde Ag | Verfahren zum Verflüssigen eines Kohlenwasserstoff-reichen Stromes |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1619728C3 (de) * | 1967-12-21 | 1974-02-07 | Linde Ag, 6200 Wiesbaden | Tieftemperaturrektifikations verfahren zum Trennen von Gasgemischen aus Bestandteilen, deren Siedetemperaturen weit auseinanderliegen |
DE3531307A1 (de) * | 1985-09-02 | 1987-03-05 | Linde Ag | Verfahren zur abtrennung von c(pfeil abwaerts)2(pfeil abwaerts)(pfeil abwaerts)+(pfeil abwaerts)-kohlenwasserstoffen aus erdgas |
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 (ru) * | 2005-08-23 | 2007-04-20 | Михаил Васильевич Кнатько | Способ сжижения природного газа |
-
2009
- 2009-02-10 DE DE102009008230A patent/DE102009008230A1/de not_active Withdrawn
-
2010
- 2010-01-12 AR ARP100100071A patent/AR075133A1/es active IP Right Grant
- 2010-02-02 PE PE2011001423A patent/PE20120675A1/es active IP Right Grant
- 2010-02-02 WO PCT/EP2010/000614 patent/WO2010091804A2/de active Application Filing
- 2010-02-02 CN CN201080007356.8A patent/CN102449419B/zh active Active
- 2010-02-02 BR BRPI1008539-4A patent/BRPI1008539B1/pt active IP Right Grant
- 2010-02-02 AU AU2010213188A patent/AU2010213188B2/en active Active
- 2010-02-02 RU RU2011137411/06A patent/RU2537480C2/ru active
- 2010-02-02 MY MYPI2011003699A patent/MY159967A/en unknown
-
2011
- 2011-08-10 CL CL2011001938A patent/CL2011001938A1/es unknown
- 2011-09-08 NO NO20111214A patent/NO20111214A1/no not_active Application Discontinuation
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19722490C1 (de) | 1997-05-28 | 1998-07-02 | Linde Ag | Verfahren zum Verflüssigen eines Kohlenwasserstoff-reichen Stromes |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20120198883A1 (en) * | 2011-02-08 | 2012-08-09 | Linde Aktiengesellschaft | Method for cooling a single-component or multi-component stream |
EP2484999A3 (de) * | 2011-02-08 | 2017-03-08 | Linde Aktiengesellschaft | Verfahren zum Abkühlen eines ein-oder mehrkomponentigen Stromes |
US20150096326A1 (en) * | 2013-10-08 | 2015-04-09 | Linde Aktiengesellschaft | Method for liquefying a hydrocarbon-rich fraction |
AU2014240354B2 (en) * | 2013-10-08 | 2019-07-04 | Linde Aktiengesellschaft | Method for liquefying a hydrocarbon-rich fraction |
US20160109177A1 (en) * | 2014-10-16 | 2016-04-21 | General Electric Company | System and method for natural gas liquefaction |
US10465982B2 (en) | 2014-10-16 | 2019-11-05 | General Electric Company | Method for natural gas liquefaction and filtration of solidified carbon dioxide |
WO2016134815A1 (de) * | 2015-02-26 | 2016-09-01 | Linde Aktiengesellschaft | Verfahren zur verflüssigen von erdgas |
DE102015004125A1 (de) * | 2015-03-31 | 2016-10-06 | Linde Aktiengesellschaft | Verfahren zum Verflüssigen einer Kohlenwasserstoff-reichen Fraktion |
Also Published As
Publication number | Publication date |
---|---|
BRPI1008539A2 (pt) | 2016-03-15 |
MY159967A (en) | 2017-02-15 |
CL2011001938A1 (es) | 2011-10-28 |
PE20120675A1 (es) | 2012-06-03 |
AU2010213188B2 (en) | 2015-12-24 |
BRPI1008539B1 (pt) | 2020-08-04 |
RU2011137411A (ru) | 2013-03-20 |
WO2010091804A2 (de) | 2010-08-19 |
WO2010091804A3 (de) | 2012-09-20 |
RU2537480C2 (ru) | 2015-01-10 |
AU2010213188A1 (en) | 2011-08-18 |
NO20111214A1 (no) | 2011-09-08 |
AR075133A1 (es) | 2011-03-09 |
CN102449419B (zh) | 2015-10-07 |
CN102449419A (zh) | 2012-05-09 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE69826459T2 (de) | Trennverfahren für Kohlenwasserstoffbestandteile | |
DE1551562C3 (de) | Verfahren zur Gewinnung einer methanreichen unter Druck stehenden Flüssigkeit aus verflüssigtem Naturgas | |
EP2386814B1 (de) | Stickstoff-Abtrennung aus Erdgas | |
DE102010011052A1 (de) | Verfahren zum Verflüssigen einer Kohlenwasserstoff-reichen Fraktion | |
DE102010044646A1 (de) | Verfahren zum Abtrennen von Stickstoff und Wasserstoff aus Erdgas | |
DE102009008230A1 (de) | Verfahren zum Verflüssigen eines Kohlenwasserstoff-reichen Stromes | |
EP1864062A1 (de) | Verfahren zum verflüssigen eines kohlenwasserstoff-reichen stromes | |
WO2007045364A2 (de) | Rückgewinnungssystem für die weiterverarbeitung eines spaltqasstroms einer ethylenanlage | |
WO2016128110A1 (de) | Kombinierte abtrennung von schwer- und leichtsiedern aus erdgas | |
DE102007010032A1 (de) | Verfahren zum Abtrennen von Stickstoff aus verflüssigtem Erdgas | |
DE102013013883A1 (de) | Kombinierte Abtrennung von Schwer- und Leichtsiedern aus Erdgas | |
DE10226596A1 (de) | Verfahren zum Verflüssigen eines Kohlenwasserstoff-reichen Stromes mit gleichzeitiger Gewinnung einer C3+-reichen Fraktion mit hoher Ausbeute | |
WO2010112206A2 (de) | Verfahren zum verflüssigen einer kohlenwasserstoff-reichen fraktion | |
WO2017054929A1 (de) | Verfahren zum verflüssigen einer kohlenwasserstoff-reichen fraktion | |
DE19612173C1 (de) | Verfahren zum Verflüssigen eines kohlenwasserstoffreichen Einsatzstromes | |
DE102012017485A1 (de) | Verfahren zum Abtrennen von C2+-Kohlenwasserstoffen oder von C3+-Kohlenwasserstoffen aus einer Kohlenwasserstoff-reichen Fraktion | |
DE102006021620B4 (de) | Vorbehandlung eines zu verflüssigenden Erdgasstromes | |
DE102012020469A1 (de) | Verfahren und Vorrichtung zur Abtrennung von Methan aus einem Synthesegas | |
DE102009004109A1 (de) | Verfahren zum Verflüssigen einer Kohlenwasserstoff-reichen Fraktion | |
EP1913319A2 (de) | Verfahren und anlage zum verflüssigen eines kohlenwasserstoffreichen stroms | |
DE102007006370A1 (de) | Verfahren zum Verflüssigen eines Kohlenwasserstoff-reichen Stromes | |
DE102009009477A1 (de) | Verfahren zum Abtrennen von Stickstoff | |
WO2016155863A1 (de) | Verfahren zum abtrennen von stickstoff aus einer kohlenwasserstoff-reichen fraktion | |
DE102012017486A1 (de) | Verfahren zum Abtrennen von C2+-Kohlenwasserstoffen aus einer Kohlenwasserstoff-reichen Fraktion | |
DE102004032710A1 (de) | Verfahren zum Verflüssigen eines Kohlenwasserstoff-reichen Stromes |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
R119 | Application deemed withdrawn, or ip right lapsed, due to non-payment of renewal fee |
Effective date: 20110901 |