EP0535752B1 - Verfahren zur Verflüssigung von Erdgas - Google Patents
Verfahren zur Verflüssigung von Erdgas Download PDFInfo
- Publication number
- EP0535752B1 EP0535752B1 EP92203009A EP92203009A EP0535752B1 EP 0535752 B1 EP0535752 B1 EP 0535752B1 EP 92203009 A EP92203009 A EP 92203009A EP 92203009 A EP92203009 A EP 92203009A EP 0535752 B1 EP0535752 B1 EP 0535752B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- pressure
- zone
- gas
- phase
- methane
- 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.)
- Expired - Lifetime
Links
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims description 78
- 238000000034 method Methods 0.000 title claims description 22
- 239000003345 natural gas Substances 0.000 title claims description 12
- 239000007789 gas Substances 0.000 claims description 43
- 238000005194 fractionation Methods 0.000 claims description 31
- 239000012071 phase Substances 0.000 claims description 24
- 239000007791 liquid phase Substances 0.000 claims description 21
- 238000001816 cooling Methods 0.000 claims description 16
- 229930195733 hydrocarbon Natural products 0.000 claims description 13
- 150000002430 hydrocarbons Chemical class 0.000 claims description 13
- 239000007788 liquid Substances 0.000 claims description 13
- 239000007792 gaseous phase Substances 0.000 claims description 10
- 239000012530 fluid Substances 0.000 claims description 8
- 238000009834 vaporization Methods 0.000 claims description 4
- 230000008016 vaporization Effects 0.000 claims description 4
- 239000004215 Carbon black (E152) Substances 0.000 claims description 3
- 230000000295 complement effect Effects 0.000 claims description 2
- 238000007906 compression Methods 0.000 claims description 2
- 230000006835 compression Effects 0.000 claims description 2
- 238000004821 distillation Methods 0.000 claims description 2
- 230000007423 decrease Effects 0.000 claims 5
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 14
- 239000000203 mixture Substances 0.000 description 9
- 239000001294 propane Substances 0.000 description 7
- 238000010992 reflux Methods 0.000 description 7
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 5
- 239000002912 waste gas Substances 0.000 description 4
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical class S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 239000003507 refrigerant Substances 0.000 description 2
- 239000012808 vapor phase Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000000155 melt Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Images
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
- F25J1/0032—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 the feed stream itself or separated fractions from it, i.e. "internal refrigeration"
- F25J1/0035—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 the feed stream itself or separated fractions from it, i.e. "internal refrigeration" by gas expansion with extraction of work
-
- 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
-
- 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
- F25J1/0214—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 dual level refrigeration cascade with at least one 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
- F25J1/0211—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
- F25J1/0214—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 dual level refrigeration cascade with at least one MCR cycle
- F25J1/0215—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 dual level refrigeration cascade with at least one MCR cycle with one SCR cycle
- F25J1/0216—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 dual level refrigeration cascade with at least one MCR cycle with one SCR cycle using a C3 pre-cooling 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
- F25J1/0228—Coupling of the liquefaction unit to other units or processes, so-called integrated processes
- F25J1/0235—Heat exchange integration
- F25J1/0237—Heat exchange integration integrating refrigeration provided for liquefaction and purification/treatment of the gas to be liquefied, e.g. heavy hydrocarbon removal from natural gas
- F25J1/0239—Purification or treatment step being integrated between two refrigeration cycles of a refrigeration cascade, i.e. first cycle providing feed gas cooling and second cycle providing overhead gas cooling
-
- 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.
- F25J1/0292—Refrigerant compression by cold or cryogenic suction of the refrigerant 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
- F25J3/0204—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
- F25J3/0242—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
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/04—Processes or apparatus using separation by rectification in a dual 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
- F25J2200/72—Refluxing the column with at least a part of the totally condensed overhead 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
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/74—Refluxing the column with at least a part of the partially condensed overhead 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
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/78—Refluxing the column with a liquid stream originating from an upstream or downstream fractionator column
-
- 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
- F25J2220/00—Processes or apparatus involving steps for the removal of impurities
- F25J2220/60—Separating impurities from natural gas, e.g. mercury, cyclic 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
- F25J2220/00—Processes or apparatus involving steps for the removal of impurities
- F25J2220/60—Separating impurities from natural gas, e.g. mercury, cyclic hydrocarbons
- F25J2220/66—Separating acid gases, e.g. CO2, SO2, H2S or RSH
-
- 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
- F25J2235/00—Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams
- F25J2235/60—Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams the fluid being (a 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
- 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
- F25J2270/00—Refrigeration techniques used
- F25J2270/66—Closed external refrigeration cycle with multi component refrigerant [MCR], e.g. mixture of hydrocarbons
Definitions
- the invention relates to a natural gas liquefaction process comprising the separation of hydrocarbons heavier than methane.
- Natural gas and other methane-rich gas streams are commonly available at sites away from places of use, and it is therefore common to liquefy natural gas for transportation by land or sea. Liquefaction is widely practiced in the present day and the literature and patents describe numerous processes and apparatuses for liquefaction. US-A-3945 214, 4251 247, 4274 849, 4339 253 and 4539 028 are examples of such methods.
- US Pat. No. 4,690,702 describes a process in which the charge of hydrocarbons under high pressure (P1) is cooled so as to cause the liquefaction of part of the hydrocarbons, a gas phase (G1) is separated from a liquid phase (L1), the gas phase is relaxed (G1) to lower its pressure to a value (P2) lower than (P1), the liquid phase (L1) and the gas phase (G1) are sent under pressure (P2) in a first fractionation zone, for example a purification column - contact refrigeration, a residual gas (G2) rich in methane is drawn off at the head, the pressure of which is then raised to a value (P3), it is withdrawn in melts a liquid phase (L2), the phase (L2) is sent to a second fractionation zone, for example a fractionation column, a liquid phase is drawn off at the bottom (L3), enriched in higher hydrocarbons, for example C3 +, a gas phase (G3) is drawn off at the head, at least part of the gas phase
- the expansion of G1 takes place in a turboexpander which transmits at least part of the energy collected to a turbocharger which raises the pressure of G2 to the value P3.
- the process of the invention is distinguished, for its fractionation part, from the process of US-A-4 690 702, in that the pressures used in the fractionation zones are higher than those previously used and in that the second fractionation zone operates at a lower pressure than the first fractionation zone.
- US Pat. No. 4,657,571 discloses a process corresponding to the preamble of claim 1.
- the gaseous charge of hydrocarbons containing methane and at least one hydrocarbon heavier than methane, under pressure P1 is cooled in one or more stages so as to form at least one gaseous phase G1, the gas phase G1 to lower its pressure from the value P1 to a value P2 lower than P1, the pressure reduction product P la is sent to a first contact fractionation zone, a residual gas G2 enriched in methane is drawn off at the head , a liquid phase L2 is drawn off at the bottom, the liquid phase L2 is sent to a second fractionation zone by distillation operating under a pressure P4 lower than the pressure P2 of the first fractionation zone, it is drawn off at the bottom thereof at least one liquid phase L3, enriched in hydrocarbons heavier than methane, a gas phase G3 is drawn off at the head and it is returned to the first fractionation zone as reflux.
- At least part of the gas phase G3 is condensed, to produce a condensed phase L4 and the pressure of at least part of the condensed phase L4 is raised, which is sent to the first zone fractionation as reflux and the residual gas G2 is then further cooled under a pressure at least equal to P2; in a methane liquefaction zone, so as to obtain a methane-rich liquid.
- the gas is initially available under a pressure P1 of at least 5 MPa, preferably at least 6 MPa.
- P2 0.3 to 0.8 P1
- P2 being chosen for example between 3.5 and 7 MPa, preferably between 4.5 and 6 MPa.
- the expansion of G1 is done in one or more turboexpanders coupled (s) to one or more turbocharger (s) which recompresses (s) the waste gas G2 from the pressure P2 to a pressure P3.
- At least one liquid phase L1 is formed in addition to the gas phase G1, and the liquid phase L1 is sent, after expansion, to said first fractionation zone by contact.
- the gas phase G3 is completely condensed and a portion is sent to the second fractionation zone as internal reflux and the complement to the first fractionation zone as reflux.
- the condensation can be completed by further compressing, with subsequent cooling of the said G3 phase.
- the invention is illustrated by the attached figure.
- the natural gas from line 1 passes through one or more exchangers 2, for example of the propane or C connection / C3 liquid mixture type, and advantageously one or more exchangers using cold process fluids.
- the cold fluid comes from line 5 of the first contact column 7.
- the gas which here is partially liquefied, is fractionated in the flask 4 into liquid conveyed to column 7 via line 6 equipped with a valve.
- the expansion causes partial liquefaction of the gas and the product of the expansion is sent by line 10 to column 7.
- This column is of a conventional type, for example at trays or filled. It includes a reboiling circuit 11.
- the liquid effluent from the bottom of the column is expanded by the valve 12 and sent by line 13 to column 14.
- This column which operates at a lower pressure than column 7, has a reboiler 15.
- the vapors are partly or completely condensed in the condenser 17.
- the phase resulting liquid is returned at least in part to column 14 as reflux by line 18.
- the gas phase (line 19 and valve V2) is then condensed, preferably entirely, by cooling preferably in the exchanger 20 supplied by minus part of the residual gas at the top of column 7 (lines 21 and 22).
- valve V2 is closed if all of the vapor phase has been condensed in 17.
- the valve V3 is open and it is then the liquid phase which is sent to column 7 via line 19a. You can also open the 2 valves V2 and V3 and thus send a mixed phase.
- the liquid phase resulting from the cooling in the exchanger 20 passes into the balloon 23, the recompression pump 24 and returns to column 7 via line 25 as reflux. If the condensation in the exchanger 20 is not total, which is less preferred, the residual gas can be evacuated by line 26.
- the waste gas coming from the head of column 7 by line 21, in the form of the aforementioned embodiment, passes through the exchanger 20 before being sent to the turbocharger 27 via the lines 28 and 29.
- the turbocharger is driven by the turboexpander 9.
- At least part of the waste gas from line 21 is sent via line 30 to the exchanger 3 to cool the natural gas. It then joins the turbocharger 27 via lines 5 and 29.
- the waste gas (line 21) passes successively through the exchangers 20 and 3, or vice versa, before joining the turbocharger 27.
- the gas is sent via line 32, which may include one or more exchangers, not shown, to a conventional methane liquefaction unit, shown here in a simplified manner. It passes through a first cooling exchanger 33, then the expansion valve V4 and a second cooling exchanger 34 where the liquefaction and subcooling are completed.
- the refrigerant circuit of conventional or improved type (one can for example use the circuit of US-A-4 274 849) is shown here by the use of a multi-component fluid for example a mixture of nitrogen, methane , ethane and propane, initially in the gaseous state (line 35), which is compressed by one or more compressors such as 36, cooled by the external medium, air or water, in one or more exchangers such as 37, further cooled in exchanger 38, for example with propane or a C2 / C3 liquid mixture.
- a multi-component fluid for example a mixture of nitrogen, methane , ethane and propane, initially in the gaseous state (line 35), which is compressed by one or more compressors such as 36, cooled by the external medium, air or water, in one or more exchangers such as 37, further cooled in exchanger 38, for example with propane or a C2 / C3 liquid mixture.
- the partially condensed mixture reaches the flask 40 through line 39.
- the liquid phase passes through line 41 in the exchanger 33, is expanded by the valve 42 and returns to line 35 through the exchanger 33 where it heats up in cooling the streams 32 and 41.
- the vapor phase of the tank 40 (line 43) passes through the exchangers 33 and 34, where it is condensed, then is expanded in the valve 44 and passes through the exchangers 34 and 33 via the lines 45 and 35.
- the liquefaction of methane is carried out by indirect contact with one or more fractions of a multicomponent fluid during vaporization and circulating in a closed circuit comprising compression, cooling with liquefaction giving one or more condensates and vaporization. said condensates constituting said multicomponent fluid.
- a natural gas having the following composition is treated, in mol%: Methane 90.03 Ethane 5.50 Propane 2.10 C4 - C6 2.34 Mercaptans 0.03 100.00 under a pressure of 8 MPa.
- Reductory gas leaves column 7 at -63 ° C and it is directed partly towards the exchanger 3 and partly towards the exchanger 20. After recompression in 27 using only the energy of the turboexpander 9, the gas pressure is 5.93 MPa.
- This gas the temperature of which is -28 ° C., has the following% molar composition: Methane 93.90 Ethane 5.51 Propane 0.53 C4 - C6 Mercaptans less than 10 ppm 0.06 100.00
- This current represents 95.88 mol% of the load current of the installation.
- Liquefaction takes place as follows: The gas is cooled and condensed to -126 ° C in a first bundle of the heat exchanger 33 then expanded to 1.4 MPa and sub-cooled in a second bundle of the heat exchanger 34 to at -160 ° C. From there it is sent to storage.
- the refrigerant has the following molar composition: N2 7% Methane 38% Ethane 41% Propane 14%
- This fluid is compressed to 4.97 MPa, cooled to 40 ° C in a water exchanger 37, then cooled to -25 ° C in the exchangers represented diagrammatically by 38 in indirect contact with a liquid mixture C2 / C3, then fractionated in the separator 40 giving the liquid 41 and gas 43 phases.
- the gas phase is condensed and cooled to -126 ° C in a second bundle of the exchanger 33 then sub-cooled to -160 ° C in a bundle of the exchanger 34.
- the pressure is 0.3 MPa and the temperature is -28 ° C.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Compounds Of Unknown Constitution (AREA)
Claims (9)
- Verfahren zur Verflüssigung von Erdgas, bei dem das genannte Gas, das Methan und Kohlenwasserstoffe, die schwerer sind als das Methan unter einem Druck P₁ enthält, abkühlt, um wenigstens eine Gasphase G₁ zu bilden, die Gasphase G₁ entspannt wird, um seinen Druck zu senken und diesen auf einen Wert P₂, der kleiner ist als P₁, zu bringen, das Produkt der Entspannung unter dem Druck P₂ in eine erste Zone zur Fraktionierung durch Kontakt gesandt wird, am Kopf ein mit Methan angereichertes Restgas G₂ abgezogen wird, am Boden eine Flüssigkeitsphase L₂ abgezogen wird, die Flüssigkeitsphase L₂ in eine zweite Zone zur Fraktionierung durch Distillation, die unter einem Druck P₄ erfolgt, der kleiner ist als der Druck P₂ der ersten Fraktionierungszone, gesandt wird, man am Boden der genannten zweiten Fraktionierungszone wenigstens eine Flüssigkeitsphase L₃ entnimmt, die an Kohlenwasserstoffen, die schwerer sind als das Methan, angereichert ist, man am Kopf der genannten zweiten Fraktionierungszone eine Gasphase G₃ entnimmt und diese in die erste Fraktionierungszone als Rückfluß zurückgesandt wird, dadurch gekennzeichnet, dass man die genannte Zurücksendung ausführt, indem wenigstens ein Teil der Gasphase G₃ kondensiert wird, um eine kondensierte Phase L₄ zu bilden, und indem der Druck wenigstens eines Teils der kondensierten Phase L₄ erhöht wird, die man als Rückfluß in die genannte erste Fraktionierungszone schickt, und dass man danach das Restgas G₂ unter einem Druck, der wenigstens gleich P₂ ist, in einer Zone zur Verflüssigung des Methans weiter abkühlt, um eine an Methan reiche Flüssigkeit zu erhalten.
- Verfahren nach Anspruch 1, bei dem man die Entspannung der Gasphase G₁ in einem Turboentspanner durchführt und man eine Druckerhöhung des Restgases von dem Wert P₂ auf einen Wert P₃ in einem Turbokompressor durchführt und die von der Entspannung gelieferte Energie nutzt, um den Turbokompressor anzutreiben.
- Verfahren nach Anspruch 1 oder 2, in dem der Druck P₁ wenigstens 5 MPa beträgt, der Druck P₂ so ist, dass P₂ = 0,3 bis 0,8 P₁ ist, mit P₂ zwischen 3,5 und 7 MPa, und der Druck P₄ so ist, dass P₄ = 0,3 bis 0,9 P₂, mit P₄ zwischen 0,5 und 4,5 MPa ist.
- Verfahren nach Anspruch 3, bei dem P₁ wenigstens gleich 6 MPa ist, P₂ zwischen 4,5 und 6 MPa liegt und P₄ zwischen 2,5 und 3,5 MPa liegt.
- Verfahren nach einem der Ansprüche 1 bis 4, bei dem wenigstens ein Teil des Restgases G₂ vor der Erhöhung des Drucks des genannten Gases G₂ von P₂ auf P₃ Wärme mit dem Erdgas austauscht, um zu dessen Abkühlung beizutragen.
- Verfahren nach einem der Ansprüche 1 bis 5, bei dem wenigstens ein Teil des Restgases G₂ Wärme mit wenigstens einem Teil der Gasphase G₃ austauscht, um diese abzukühlen und um die kondensierte Phase L₄ zu erzeugen.
- Verfahren nach einem der Ansprüche 1 bis 6, bei dem die Verflüssigung des Methans durch indirektes Inberührungbringen mit einer oder mit mehreren Fraktionen eines Mehrkomponentenfluids während der Verdampfung und mit Umlauf in einem geschlossenen Kreis bewirkt wird, der eine Verdichtungszone, eine Abkühlungszone mit Verflüssigung, die ein oder mehrere Kondensate ergibt, und eine Verdampfungszone der genannten Kondensate zur Wiederherstellung des genannten Mehrkomponentenfluids besitzt.
- Verfahren nach einem der Ansprüche 1 bis 7, bei dem während der anfänglichen Abkühlung des Gases wenigstens eine Flüssigkeitsphase L₁ zusätzlich zu der Gasphase G₁ gebildet wird und man die Flüssigkeitsphase L₁ nach der Entspannung in die genannte erste Fraktionierungszone schickt.
- Verfahren nach einem der Ansprüche 1 bis 8, bei dem man die Gasphase G₃ vollständig kondensiert und man einen Teil als inneren Rückfluß in die zweite Fraktionierungszone und das Komplement als Rückfluß in die erste Fraktionierungszone geschickt wird.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR9112007 | 1991-09-30 | ||
FR9112007A FR2681859B1 (fr) | 1991-09-30 | 1991-09-30 | Procede de liquefaction de gaz naturel. |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0535752A1 EP0535752A1 (de) | 1993-04-07 |
EP0535752B1 true EP0535752B1 (de) | 1995-11-22 |
Family
ID=9417426
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP92203009A Expired - Lifetime EP0535752B1 (de) | 1991-09-30 | 1992-09-30 | Verfahren zur Verflüssigung von Erdgas |
Country Status (16)
Country | Link |
---|---|
US (1) | US5291736A (de) |
EP (1) | EP0535752B1 (de) |
JP (1) | JP3187160B2 (de) |
AR (1) | AR247945A1 (de) |
AU (1) | AU648695B2 (de) |
CA (1) | CA2079407C (de) |
DE (1) | DE69206232T2 (de) |
DZ (1) | DZ1625A1 (de) |
EG (1) | EG20248A (de) |
ES (1) | ES2089373T3 (de) |
FR (1) | FR2681859B1 (de) |
MY (1) | MY107837A (de) |
NO (1) | NO177840C (de) |
NZ (1) | NZ244542A (de) |
RU (1) | RU2093765C1 (de) |
SA (1) | SA92130161B1 (de) |
Families Citing this family (78)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5473900A (en) * | 1994-04-29 | 1995-12-12 | Phillips Petroleum Company | Method and apparatus for liquefaction of natural gas |
US5537827A (en) * | 1995-06-07 | 1996-07-23 | Low; William R. | Method for liquefaction of natural gas |
TR199801906T2 (xx) * | 1996-03-26 | 1999-01-18 | Phillips Petroleum Company | Metan bazl� bir besleme maddesinden kondensasyon ve s�y�rma sureti ile aromatik maddelerin ve/veya a��r maddelerin bertaraf edilmesi. |
TW366411B (en) * | 1997-06-20 | 1999-08-11 | Exxon Production Research Co | Improved process for liquefaction of natural gas |
TW366410B (en) * | 1997-06-20 | 1999-08-11 | Exxon Production Research Co | Improved cascade refrigeration process for liquefaction of natural gas |
DZ2533A1 (fr) * | 1997-06-20 | 2003-03-08 | Exxon Production Research Co | Procédé perfectionné de réfrigération à constituants pour la liquéfaction de gaz naturel. |
FR2772896B1 (fr) * | 1997-12-22 | 2000-01-28 | Inst Francais Du Petrole | Procede de liquefaction d'un gaz notamment un gaz naturel ou air comportant une purge a moyenne pression et son application |
WO2001088447A1 (en) * | 2000-05-18 | 2001-11-22 | Phillips Petroleum Company | Enhanced ngl recovery utilizing refrigeration and reflux from lng plants |
US6401486B1 (en) * | 2000-05-18 | 2002-06-11 | Rong-Jwyn Lee | Enhanced NGL recovery utilizing refrigeration and reflux from LNG plants |
DE10027903A1 (de) * | 2000-06-06 | 2001-12-13 | Linde Ag | Verfahren zum Gewinnen einer C¶2¶¶+¶-reichen Fraktion |
AU7158701A (en) * | 2000-08-11 | 2002-02-25 | Fluor Corp | High propane recovery process and configurations |
FR2821351B1 (fr) * | 2001-02-26 | 2003-05-16 | Technip Cie | Procede de recuperation d'ethane, mettant en oeuvre un cycle de refrigeration utilisant un melange d'au moins deux fluides refrigerants, gaz obtenus par ce procede, et installation de mise en oeuvre |
US7219512B1 (en) | 2001-05-04 | 2007-05-22 | Battelle Energy Alliance, Llc | Apparatus for the liquefaction of natural gas and methods relating to same |
US7591150B2 (en) * | 2001-05-04 | 2009-09-22 | Battelle Energy Alliance, Llc | Apparatus for the liquefaction of natural gas and methods relating to same |
US7594414B2 (en) * | 2001-05-04 | 2009-09-29 | Battelle Energy Alliance, Llc | Apparatus for the liquefaction of natural gas and methods relating to same |
US20070137246A1 (en) * | 2001-05-04 | 2007-06-21 | Battelle Energy Alliance, Llc | Systems and methods for delivering hydrogen and separation of hydrogen from a carrier medium |
US7637122B2 (en) * | 2001-05-04 | 2009-12-29 | Battelle Energy Alliance, Llc | Apparatus for the liquefaction of a gas and methods relating to same |
US6581409B2 (en) | 2001-05-04 | 2003-06-24 | Bechtel Bwxt Idaho, Llc | Apparatus for the liquefaction of natural gas and methods related to same |
US6742358B2 (en) * | 2001-06-08 | 2004-06-01 | Elkcorp | Natural gas liquefaction |
UA76750C2 (uk) * | 2001-06-08 | 2006-09-15 | Елккорп | Спосіб зрідження природного газу (варіанти) |
US6564580B2 (en) * | 2001-06-29 | 2003-05-20 | Exxonmobil Upstream Research Company | Process for recovering ethane and heavier hydrocarbons from methane-rich pressurized liquid mixture |
CN100422675C (zh) * | 2001-09-11 | 2008-10-01 | 中国石油化工股份有限公司 | 一种改进的轻烃深冷分离方法 |
US6823692B1 (en) | 2002-02-11 | 2004-11-30 | Abb Lummus Global Inc. | Carbon dioxide reduction scheme for NGL processes |
AU2002303849B2 (en) * | 2002-05-20 | 2006-05-25 | Fluor Technologies Corporation | Twin reflux process and configurations for improved natural gas liquids recovery |
US6945075B2 (en) * | 2002-10-23 | 2005-09-20 | Elkcorp | Natural gas liquefaction |
US6793712B2 (en) * | 2002-11-01 | 2004-09-21 | Conocophillips Company | Heat integration system for natural gas liquefaction |
CA2515999C (en) * | 2003-02-25 | 2012-12-18 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing |
US6889523B2 (en) | 2003-03-07 | 2005-05-10 | Elkcorp | LNG production in cryogenic natural gas processing plants |
US6662589B1 (en) | 2003-04-16 | 2003-12-16 | Air Products And Chemicals, Inc. | Integrated high pressure NGL recovery in the production of liquefied natural gas |
FR2855526B1 (fr) * | 2003-06-02 | 2007-01-26 | Technip France | Procede et installation de production simultanee d'un gaz naturel apte a etre liquefie et d'une coupe de liquides du gaz naturel |
US7155931B2 (en) * | 2003-09-30 | 2007-01-02 | Ortloff Engineers, Ltd. | Liquefied natural gas processing |
WO2005045338A1 (en) * | 2003-10-30 | 2005-05-19 | Fluor Technologies Corporation | Flexible ngl process and methods |
US7159417B2 (en) * | 2004-03-18 | 2007-01-09 | Abb Lummus Global, Inc. | Hydrocarbon recovery process utilizing enhanced reflux streams |
US7204100B2 (en) * | 2004-05-04 | 2007-04-17 | Ortloff Engineers, Ltd. | Natural gas liquefaction |
ES2284429T1 (es) * | 2004-07-01 | 2007-11-16 | Ortloff Engineers, Ltd | Procesamiento de gas natural licuado. |
US20060260355A1 (en) * | 2005-05-19 | 2006-11-23 | Roberts Mark J | Integrated NGL recovery and liquefied natural gas production |
US9080810B2 (en) * | 2005-06-20 | 2015-07-14 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing |
US20070056318A1 (en) * | 2005-09-12 | 2007-03-15 | Ransbarger Weldon L | Enhanced heavies removal/LPG recovery process for LNG facilities |
US9726425B2 (en) * | 2006-04-12 | 2017-08-08 | Shell Oil Company | Method and apparatus for liquefying a natural gas stream |
EP2024700A2 (de) * | 2006-06-02 | 2009-02-18 | Ortloff Engeneers, Ltd | Verarbeitung von flüssigerdgas |
WO2007144395A2 (en) | 2006-06-16 | 2007-12-21 | Shell Internationale Research Maatschappij B.V. | Method and apparatus for treating a hydrocarbon stream |
JP2010507702A (ja) * | 2006-10-24 | 2010-03-11 | シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ | 精製液化天然ガスの製造方法 |
US8590340B2 (en) * | 2007-02-09 | 2013-11-26 | Ortoff Engineers, Ltd. | Hydrocarbon gas processing |
US8028724B2 (en) | 2007-02-12 | 2011-10-04 | Daewoo Shipbuilding & Marine Engineering Co., Ltd. | LNG tank and unloading of LNG from the tank |
US9869510B2 (en) * | 2007-05-17 | 2018-01-16 | Ortloff Engineers, Ltd. | Liquefied natural gas processing |
US8555672B2 (en) * | 2009-10-22 | 2013-10-15 | Battelle Energy Alliance, Llc | Complete liquefaction methods and apparatus |
US8899074B2 (en) | 2009-10-22 | 2014-12-02 | Battelle Energy Alliance, Llc | Methods of natural gas liquefaction and natural gas liquefaction plants utilizing multiple and varying gas streams |
US8061413B2 (en) | 2007-09-13 | 2011-11-22 | Battelle Energy Alliance, Llc | Heat exchangers comprising at least one porous member positioned within a casing |
US9254448B2 (en) | 2007-09-13 | 2016-02-09 | Battelle Energy Alliance, Llc | Sublimation systems and associated methods |
US9574713B2 (en) | 2007-09-13 | 2017-02-21 | Battelle Energy Alliance, Llc | Vaporization chambers and associated methods |
US9217603B2 (en) | 2007-09-13 | 2015-12-22 | Battelle Energy Alliance, Llc | Heat exchanger and related methods |
US8919148B2 (en) * | 2007-10-18 | 2014-12-30 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing |
FR2923000B1 (fr) * | 2007-10-26 | 2015-12-11 | Inst Francais Du Petrole | Procede de liquefaction d'un gaz naturel avec recuperation amelioree de propane. |
US7644676B2 (en) | 2008-02-11 | 2010-01-12 | Daewoo Shipbuilding & Marine Engineering Co., Ltd. | Storage tank containing liquefied natural gas with butane |
KR20090107805A (ko) | 2008-04-10 | 2009-10-14 | 대우조선해양 주식회사 | 천연가스 발열량 저감방법 및 장치 |
US20090282865A1 (en) | 2008-05-16 | 2009-11-19 | Ortloff Engineers, Ltd. | Liquefied Natural Gas and Hydrocarbon Gas Processing |
FR2943683B1 (fr) * | 2009-03-25 | 2012-12-14 | Technip France | Procede de traitement d'un gaz naturel de charge pour obtenir un gaz naturel traite et une coupe d'hydrocarbures en c5+, et installation associee |
US8434325B2 (en) | 2009-05-15 | 2013-05-07 | Ortloff Engineers, Ltd. | Liquefied natural gas and hydrocarbon gas processing |
US20100287982A1 (en) * | 2009-05-15 | 2010-11-18 | Ortloff Engineers, Ltd. | Liquefied Natural Gas and Hydrocarbon Gas Processing |
US9021832B2 (en) * | 2010-01-14 | 2015-05-05 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing |
AU2011261670B2 (en) | 2010-06-03 | 2014-08-21 | Uop Llc | Hydrocarbon gas processing |
US10451344B2 (en) | 2010-12-23 | 2019-10-22 | Fluor Technologies Corporation | Ethane recovery and ethane rejection methods and configurations |
US10852060B2 (en) | 2011-04-08 | 2020-12-01 | Pilot Energy Solutions, Llc | Single-unit gas separation process having expanded, post-separation vent stream |
US10655911B2 (en) | 2012-06-20 | 2020-05-19 | Battelle Energy Alliance, Llc | Natural gas liquefaction employing independent refrigerant path |
RU2534832C2 (ru) * | 2012-12-11 | 2014-12-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования Казанский национальный исследовательский технический университет им. А.Н. Туполева-КАИ" (КНИТУ-КАИ) | Способ раздачи природного газа с одновременной выработкой сжиженного газа при транспортировании потребителю из магистрального трубопровода высокого давления в трубопровод низкого давления |
US10006701B2 (en) | 2016-01-05 | 2018-06-26 | Fluor Technologies Corporation | Ethane recovery or ethane rejection operation |
FR3047552A1 (fr) * | 2016-02-05 | 2017-08-11 | Air Liquide | Introduction optimisee d'un courant refrigerant mixte diphasique dans un procede de liquefaction de gaz naturel |
US10330382B2 (en) | 2016-05-18 | 2019-06-25 | Fluor Technologies Corporation | Systems and methods for LNG production with propane and ethane recovery |
US10533794B2 (en) | 2016-08-26 | 2020-01-14 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing |
US10551119B2 (en) | 2016-08-26 | 2020-02-04 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing |
US10551118B2 (en) | 2016-08-26 | 2020-02-04 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing |
CA3033088A1 (en) | 2016-09-09 | 2018-03-15 | Fluor Technologies Corporation | Methods and configuration for retrofitting ngl plant for high ethane recovery |
FR3056223B1 (fr) * | 2016-09-20 | 2020-05-01 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Procede de purification de gaz naturel a liquefier |
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 |
US11112175B2 (en) | 2017-10-20 | 2021-09-07 | Fluor Technologies Corporation | Phase implementation of natural gas liquid recovery plants |
WO2021076881A1 (en) * | 2019-10-17 | 2021-04-22 | Conocophillips Company | Standalone high-pressure heavies removal unit for lng processing |
DE102020004821A1 (de) * | 2020-08-07 | 2022-02-10 | Linde Gmbh | Verfahren und Anlage zur Herstellung eines Flüssigerdgasprodukts |
Family Cites Families (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3763658A (en) * | 1970-01-12 | 1973-10-09 | Air Prod & Chem | Combined cascade and multicomponent refrigeration system and method |
DE2110417A1 (de) * | 1971-03-04 | 1972-09-21 | Linde Ag | Verfahren zum Verfluessigen und Unterkuehlen von Erdgas |
FR2237147B1 (de) * | 1973-07-03 | 1976-04-30 | Teal Procedes Air Liquide Tech | |
FR2280041A1 (fr) * | 1974-05-31 | 1976-02-20 | Teal Technip Liquefaction Gaz | Procede et installation pour le refroidissement d'un melange gazeux |
FR2292203A1 (fr) * | 1974-11-21 | 1976-06-18 | Technip Cie | Procede et installation pour la liquefaction d'un gaz a bas point d'ebullition |
US4065278A (en) * | 1976-04-02 | 1977-12-27 | Air Products And Chemicals, Inc. | Process for manufacturing liquefied methane |
US4140504A (en) * | 1976-08-09 | 1979-02-20 | The Ortloff Corporation | Hydrocarbon gas processing |
US4185978A (en) * | 1977-03-01 | 1980-01-29 | Standard Oil Company (Indiana) | Method for cryogenic separation of carbon dioxide from hydrocarbons |
US4155729A (en) * | 1977-10-20 | 1979-05-22 | Phillips Petroleum Company | Liquid flash between expanders in gas separation |
US4203741A (en) * | 1978-06-14 | 1980-05-20 | Phillips Petroleum Company | Separate feed entry to separator-contactor in gas separation |
US4203742A (en) * | 1978-10-31 | 1980-05-20 | Stone & Webster Engineering Corporation | Process for the recovery of ethane and heavier hydrocarbon components from methane-rich gases |
FR2471566B1 (fr) * | 1979-12-12 | 1986-09-05 | Technip Cie | Procede et systeme de liquefaction d'un gaz a bas point d'ebullition |
FR2545589B1 (fr) * | 1983-05-06 | 1985-08-30 | Technip Cie | Procede et appareil de refroidissement et liquefaction d'au moins un gaz a bas point d'ebullition, tel que par exemple du gaz naturel |
US4657571A (en) * | 1984-06-29 | 1987-04-14 | Snamprogetti S.P.A. | Process for the recovery of heavy constituents from hydrocarbon gaseous mixtures |
FR2571129B1 (fr) * | 1984-09-28 | 1988-01-29 | Technip Cie | Procede et installation de fractionnement cryogenique de charges gazeuses |
US4707170A (en) * | 1986-07-23 | 1987-11-17 | Air Products And Chemicals, Inc. | Staged multicomponent refrigerant cycle for a process for recovery of C+ hydrocarbons |
-
1991
- 1991-09-30 FR FR9112007A patent/FR2681859B1/fr not_active Expired - Fee Related
-
1992
- 1992-09-29 NO NO923783A patent/NO177840C/no unknown
- 1992-09-29 EG EG57492A patent/EG20248A/xx active
- 1992-09-29 DZ DZ920127A patent/DZ1625A1/fr active
- 1992-09-29 RU SU925052813A patent/RU2093765C1/ru active
- 1992-09-29 CA CA002079407A patent/CA2079407C/en not_active Expired - Lifetime
- 1992-09-29 MY MYPI92001743A patent/MY107837A/en unknown
- 1992-09-29 NZ NZ24454292A patent/NZ244542A/en unknown
- 1992-09-30 AU AU26127/92A patent/AU648695B2/en not_active Expired
- 1992-09-30 JP JP26196992A patent/JP3187160B2/ja not_active Expired - Lifetime
- 1992-09-30 DE DE69206232T patent/DE69206232T2/de not_active Expired - Fee Related
- 1992-09-30 US US07/954,318 patent/US5291736A/en not_active Expired - Lifetime
- 1992-09-30 EP EP92203009A patent/EP0535752B1/de not_active Expired - Lifetime
- 1992-09-30 AR AR92323310A patent/AR247945A1/es active
- 1992-09-30 ES ES92203009T patent/ES2089373T3/es not_active Expired - Lifetime
- 1992-10-10 SA SA92130161A patent/SA92130161B1/ar unknown
Also Published As
Publication number | Publication date |
---|---|
NO177840B (no) | 1995-08-21 |
CA2079407C (en) | 2001-05-15 |
JP3187160B2 (ja) | 2001-07-11 |
ES2089373T3 (es) | 1996-10-01 |
NO177840C (no) | 1995-11-29 |
AU2612792A (en) | 1993-04-01 |
AU648695B2 (en) | 1994-04-28 |
FR2681859B1 (fr) | 1994-02-11 |
SA92130161B1 (ar) | 2004-05-29 |
CA2079407A1 (en) | 1993-03-31 |
NZ244542A (en) | 1994-07-26 |
FR2681859A1 (fr) | 1993-04-02 |
US5291736A (en) | 1994-03-08 |
JPH05240576A (ja) | 1993-09-17 |
DE69206232T2 (de) | 1996-07-18 |
DZ1625A1 (fr) | 2002-02-17 |
EP0535752A1 (de) | 1993-04-07 |
RU2093765C1 (ru) | 1997-10-20 |
AR247945A1 (es) | 1995-04-28 |
NO923783D0 (no) | 1992-09-29 |
EG20248A (en) | 1998-05-31 |
DE69206232D1 (de) | 1996-01-04 |
NO923783L (no) | 1993-03-31 |
MY107837A (en) | 1996-06-29 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0535752B1 (de) | Verfahren zur Verflüssigung von Erdgas | |
US6526777B1 (en) | LNG production in cryogenic natural gas processing plants | |
RU2298743C2 (ru) | Система и способ для сжижения природного газа при высоком давлении | |
CA2035620C (en) | Method of liquefying natural gas | |
EP0572590B1 (de) | Stickstoffentfernungsverfahren aus einem hauptsächlich methan enthaltenden kohlenwasserstoffeinsatzgemisch mit mindestens 2 mol % stickstoff | |
US6889523B2 (en) | LNG production in cryogenic natural gas processing plants | |
US4065278A (en) | Process for manufacturing liquefied methane | |
CA2562907C (en) | Natural gas liquefaction | |
EP0644996B1 (de) | Verfahren und anlage zur kühlung eines fluids, insbesondere für die verflüssigung von erdgas | |
EP0504029B1 (de) | Verfahren zur Herstellung von gasförmigem Sauerstoff unter Druck | |
EP0768502B1 (de) | Verfahren und Vorrichtung zur Verflüssigung und Behandlung von Erdgas | |
FR2675891A1 (fr) | Procede de production d'azote liquide en utilisant un gaz naturel liquefie comme seul refrigerant. | |
ZA200607240B (en) | Natural gas liquefaction | |
MXPA97003373A (es) | Produccion de gas natural liquido en plantas deprocesamiento de gas natural criogenico | |
EP0731900B1 (de) | Verfahren und einrichtung zur erdgasverflüssigung | |
EP0618415B1 (de) | Verfahren und Vorrichtung zur Herstellung von gasförmigem Sauerstoff und/oder gasförmigem Stickstoff unter Druck durch Zerlegung von Luft | |
WO2003038358A1 (fr) | Procede et installation de separation d'un gaz contenant du methane et de l'ethane a deux colonnes fonctionnant sous deux pressions differentes | |
EA000800B1 (ru) | Способ извлечения конденсацией и отгонкой ароматических и/или высокомолекулярных углеводородов из сырья на основе метана и устройство для его осуществления | |
EP0641983B1 (de) | Verfahren und Einrichtung zur Herstellung von gasförmigem Sauerstoff und/oder Stickstoff unter Druck | |
FR2832213A1 (fr) | Procede et installation de production d'helium | |
EP0612967B1 (de) | Verfahren zur Herstellung von Sauerstoff und/oder Stickstoff unter Druck | |
EP0641982B1 (de) | Verfahren und Einrichtung zur Herstellung von wenigstens einem durch Zerlegung von Luft gewonnenem Gas unter Druck | |
AU2004219688A1 (en) | LNG production in cryogenic natural gas processing plants |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): BE DE ES FR GB IT NL |
|
17P | Request for examination filed |
Effective date: 19930918 |
|
17Q | First examination report despatched |
Effective date: 19940513 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): BE DE ES FR GB IT NL |
|
REF | Corresponds to: |
Ref document number: 69206232 Country of ref document: DE Date of ref document: 19960104 |
|
ITF | It: translation for a ep patent filed |
Owner name: DE DOMINICIS & MAYER S.R.L. |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: BA2A Ref document number: 2089373 Country of ref document: ES Kind code of ref document: T3 |
|
GBT | Gb: translation of ep patent filed (gb section 77(6)(a)/1977) |
Effective date: 19960320 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FG2A Ref document number: 2089373 Country of ref document: ES Kind code of ref document: T3 |
|
26N | No opposition filed | ||
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FG2A Ref document number: 2089373 Country of ref document: ES Kind code of ref document: T3 |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: IF02 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20070928 Year of fee payment: 16 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20090401 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 20110824 Year of fee payment: 20 Ref country code: ES Payment date: 20110926 Year of fee payment: 20 Ref country code: FR Payment date: 20110914 Year of fee payment: 20 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: IT Payment date: 20110926 Year of fee payment: 20 Ref country code: NL Payment date: 20110822 Year of fee payment: 20 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 20110923 Year of fee payment: 20 |
|
BE20 | Be: patent expired |
Owner name: CIE FRANCAISE D'*ETUDES ET DE *CONSTRUCTION TECHNI Effective date: 20120930 |
|
REG | Reference to a national code |
Ref country code: NL Ref legal event code: V4 Effective date: 20120930 |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: PE20 Expiry date: 20120929 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION Effective date: 20120929 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FD2A Effective date: 20130718 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: ES Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION Effective date: 20121001 |