RU2009144777A - Способ сжижения природного газа - Google Patents
Способ сжижения природного газа Download PDFInfo
- Publication number
- RU2009144777A RU2009144777A RU2009144777/06A RU2009144777A RU2009144777A RU 2009144777 A RU2009144777 A RU 2009144777A RU 2009144777/06 A RU2009144777/06 A RU 2009144777/06A RU 2009144777 A RU2009144777 A RU 2009144777A RU 2009144777 A RU2009144777 A RU 2009144777A
- Authority
- RU
- Russia
- Prior art keywords
- refrigerant
- cooled
- heat exchange
- stream
- cooling
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract 21
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract 6
- 239000007788 liquid Substances 0.000 title claims 2
- 239000003345 natural gas Substances 0.000 title 1
- 239000003507 refrigerant Substances 0.000 claims abstract 34
- 238000001816 cooling Methods 0.000 claims abstract 13
- 239000012530 fluid Substances 0.000 claims abstract 6
- 238000005057 refrigeration Methods 0.000 claims abstract 2
- 239000007789 gas Substances 0.000 claims 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims 3
- 230000006835 compression Effects 0.000 claims 2
- 238000007906 compression Methods 0.000 claims 2
- 239000012809 cooling fluid Substances 0.000 claims 1
- 229910001873 dinitrogen Inorganic materials 0.000 claims 1
- 239000003949 liquefied natural gas Substances 0.000 claims 1
- 229910052757 nitrogen Inorganic materials 0.000 claims 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/006—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the refrigerant fluid used
- F25J1/008—Hydrocarbons
- F25J1/0092—Mixtures of hydrocarbons comprising possibly also minor amounts of nitrogen
-
- 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
- F25J1/0032—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"
- F25J1/004—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 flash gas recovery
-
- 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"
- F25J1/0042—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 liquid 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
- F25J1/003—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
- F25J1/005—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 expansion of a gaseous refrigerant stream 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
- F25J1/006—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the refrigerant fluid used
- F25J1/007—Primary atmospheric gases, mixtures thereof
- F25J1/0072—Nitrogen
-
- 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
- F25J1/006—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the refrigerant fluid used
- F25J1/008—Hydrocarbons
- F25J1/0082—Methane
-
- 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
- F25J1/006—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the refrigerant fluid used
- F25J1/0095—Oxides of carbon, e.g. CO2
-
- 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
- F25J1/0217—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 at least a three level refrigeration cascade with at least one MCR cycle
- F25J1/0218—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 at least a three level refrigeration cascade with at least one MCR cycle with one or more SCR cycles, e.g. with 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
- F25J1/0243—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
- F25J1/0245—Different modes, i.e. 'runs', of operation; Process control
- F25J1/0249—Controlling refrigerant inventory, i.e. composition or quantity
- F25J1/025—Details related to the refrigerant production or treatment, e.g. make-up supply from feed gas itself
-
- 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
- F25J1/0254—Operation; Control and regulation; Instrumentation controlling particular process parameter, e.g. pressure, temperature
-
- 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
- F25J1/0257—Construction and layout of liquefaction equipments, e.g. valves, machines
- F25J1/0262—Details of the cold heat exchange system
- F25J1/0264—Arrangement of heat exchanger cores in parallel with different functions, e.g. different cooling streams
- F25J1/0265—Arrangement of heat exchanger cores in parallel with different functions, e.g. different cooling streams comprising cores associated exclusively with the cooling of a refrigerant stream, e.g. for auto-refrigeration or economizer
- F25J1/0268—Arrangement of heat exchanger cores in parallel with different functions, e.g. different cooling streams comprising cores associated exclusively with the cooling of a refrigerant stream, e.g. for auto-refrigeration or economizer using a dedicated refrigeration means
-
- 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
- F25J1/0257—Construction and layout of liquefaction equipments, e.g. valves, machines
- F25J1/0275—Construction and layout of liquefaction equipments, e.g. valves, machines adapted for special use of the liquefaction unit, e.g. portable or transportable devices
- F25J1/0277—Offshore use, e.g. during shipping
- F25J1/0278—Unit being stationary, e.g. on floating barge or fixed platform
-
- 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.
- F25J1/0285—Combination of different types of drivers mechanically coupled to the same refrigerant compressor, possibly split on multiple compressor casings
- F25J1/0288—Combination of different types of drivers mechanically coupled to the same refrigerant compressor, possibly split on multiple compressor casings using work extraction by mechanical coupling of compression and expansion of the refrigerant, so-called companders
-
- 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
- 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.
- F25J1/0296—Removal of the heat of compression, e.g. within an inter- or afterstage-cooler against an ambient heat sink
- F25J1/0297—Removal of the heat of compression, e.g. within an inter- or afterstage-cooler against an ambient heat sink using an externally chilled fluid, e.g. chilled water
-
- 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
- F25J2220/00—Processes or apparatus involving steps for the removal of impurities
- F25J2220/60—Separating impurities from natural gas, e.g. mercury, cyclic hydrocarbons
- F25J2220/62—Separating low boiling components, e.g. He, H2, N2, Air
-
- 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
- F25J2230/00—Processes or apparatus involving steps for increasing the pressure of gaseous process streams
- F25J2230/04—Compressor cooling arrangement, e.g. inter- or after-stage cooling or condensate removal
-
- 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
- F25J2230/00—Processes or apparatus involving steps for increasing the pressure of gaseous process streams
- F25J2230/30—Compression 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
- F25J2270/90—External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration
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)
- Ocean & Marine Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Separation By Low-Temperature Treatments (AREA)
Abstract
1. Способ сжижения потока газа с высоким содержанием метана, содержащий этапы, при которых: ! (а) создают поток газа с абсолютным давлением менее 1200 фунтов на кв. дюйм (8273,709 кПа); ! (b) отбирают часть газа из потока для использования в качестве хладагента; ! (с) сжимают этот хладагент до давления, превышающего его давление на этапе (а) для получения сжатого хладагента; ! (d) охлаждают полученный сжатый хладагент косвенным теплообменом с охлаждающей текучей средой, имеющей температуру окружающей среды, до технологической температуры выше приблизительно 35°F (1,7°С); ! (е) подвергают охлажденный сжатый хладагент дополнительному охлаждению для дополнительного понижения его температуры, тем самым получая дополнительно охлажденный сжатый хладагент, имеющий температуру на 10-70°F (6-39°С) ниже, чем технологическая температура, получая дополнительно охлажденный, сжатый хладагент, имеющий температуру 10-60°F (6-15,6°С); ! (f) расширяют хладагент, полученный на этапе (e) для дополнительного охлаждения хладагента, получая тем самым расширенный, дополнительно охлажденный хладагент, ! (g) подают расширенный, дополнительно охлажденный хладагент в зону теплообмена и ! (h) пропускают поток газа через зону теплообмена для охлаждения по меньшей мере части потока газа путем косвенного теплообмена с расширенным, дополнительно охлажденным хладагентом, тем самым формируя поток охлажденного флюида. ! 2. Способ по п.1, при котором температура окружающей среды на этапе (d) превышает 50°F (10°C). ! 3. Способ по п.1, при котором температура окружающей среды на этапе (d) превышает 60°F (15,9°C). ! 4. Способ по п.1, при котором температура окружающей среды на этапе (d) превы
Claims (12)
1. Способ сжижения потока газа с высоким содержанием метана, содержащий этапы, при которых:
(а) создают поток газа с абсолютным давлением менее 1200 фунтов на кв. дюйм (8273,709 кПа);
(b) отбирают часть газа из потока для использования в качестве хладагента;
(с) сжимают этот хладагент до давления, превышающего его давление на этапе (а) для получения сжатого хладагента;
(d) охлаждают полученный сжатый хладагент косвенным теплообменом с охлаждающей текучей средой, имеющей температуру окружающей среды, до технологической температуры выше приблизительно 35°F (1,7°С);
(е) подвергают охлажденный сжатый хладагент дополнительному охлаждению для дополнительного понижения его температуры, тем самым получая дополнительно охлажденный сжатый хладагент, имеющий температуру на 10-70°F (6-39°С) ниже, чем технологическая температура, получая дополнительно охлажденный, сжатый хладагент, имеющий температуру 10-60°F (6-15,6°С);
(f) расширяют хладагент, полученный на этапе (e) для дополнительного охлаждения хладагента, получая тем самым расширенный, дополнительно охлажденный хладагент,
(g) подают расширенный, дополнительно охлажденный хладагент в зону теплообмена и
(h) пропускают поток газа через зону теплообмена для охлаждения по меньшей мере части потока газа путем косвенного теплообмена с расширенным, дополнительно охлажденным хладагентом, тем самым формируя поток охлажденного флюида.
2. Способ по п.1, при котором температура окружающей среды на этапе (d) превышает 50°F (10°C).
3. Способ по п.1, при котором температура окружающей среды на этапе (d) превышает 60°F (15,9°C).
4. Способ по п.1, при котором температура окружающей среды на этапе (d) превышает 70°F (21,1°C).
5. Способ по п.1, при котором перед сжатием хладагента на этапе (с), или по меньшей мере перед одной ступенью сжатия, если сжатие на этапе (с) является многоступенчатым, применяют дополнительное вспомогательное охлаждение хладагента.
6. Способ по п.2, дополнительно содержащий этапы, при которых:
(а) подают охлажденный поток флюида по п.1(h) в еще одну область теплообмена для дополнительного охлаждения;
(b) отбирают охлажденный на этапе (а) поток флюида и расширяют поток флюида для дальнейшего охлаждения;
(с) подают охлажденный на этапе (b) поток флюида на сепаратор, в котором охлажденную жидкую часть отбирают в качестве сжиженного природного газа, а паровую часть отбирают в качестве охлажденного потока пара;
(d) подают охлажденный поток пара в качестве хладагента обратно в области теплообмена по пп.6(а) и 1(g).
7. Способ по п.6, при котором часть охлажденного потока пара по п.6(с) отбирают перед прохождением через область теплообмена по п.6(а) для использования в качестве хладагента, подавая часть охлажденного потока пара во вторичный контур расширения, который проходит через области теплообмена по пп.6(а) и 1(h), сжимают на выходе из области теплообмена по п.1(h), охлаждают до температуры окружающей среды, факультативно охлаждают, пропуская через область теплообмена по п.1(h), и, затем расширяют для дальнейшего охлаждения и повторно вводят в области теплообмена по пп.6(а) и 1(g).
8. Способ по п.7, при котором охлажденный поток пара дополнительно охлаждают после охлаждения до температуры окружающей среды, но перед возвращением в область теплообмена по п.1(h).
9. Способ по п.6, при котором расширенный, дополнительно охлажденный хладагент сжимают после выхода из области теплообмена по п.1(h), охлаждают до температуры окружающей среды, факультативно охлаждают, пропуская через область теплообмена по п.1(h), и расширяют для дальнейшего охлаждения и вновь вводят в области теплообмена по пп.6(а) и 1(g).
10. Способ по п.8, при котором расширенный, дополнительно охлажденный хладагент состоит по существу из азота или газа с высоким содержанием азота.
11. Способ по п.1, при котором газовый поток по п.1(а) сжимают, охлаждают в одном или более охлаждающем устройстве, осуществляющем охлаждение до температуры окружающей среды, и далее охлаждают в дополнительном охлаждающем устройстве, при этом все указанные операции проводят перед вводом в область теплообмена по п.1(h).
12. Способ по п.1, при котором дополнительное охлаждающее устройство является внешним холодильным устройством, в котором используют внешний хладагент, при котором внешние хладагенты по существу независимы от части потока газа, используемой в качестве хладагента по п.1(b).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US92734007P | 2007-05-03 | 2007-05-03 | |
US60/927,340 | 2007-05-03 |
Publications (2)
Publication Number | Publication Date |
---|---|
RU2009144777A true RU2009144777A (ru) | 2011-06-10 |
RU2458296C2 RU2458296C2 (ru) | 2012-08-10 |
Family
ID=38596094
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
RU2009144777/06A RU2458296C2 (ru) | 2007-05-03 | 2008-03-04 | Способ сжижения природного газа |
Country Status (7)
Country | Link |
---|---|
US (1) | US8616021B2 (ru) |
AU (1) | AU2008246345B2 (ru) |
BR (1) | BRPI0808909A2 (ru) |
CA (1) | CA2681417C (ru) |
NO (1) | NO20093458L (ru) |
RU (1) | RU2458296C2 (ru) |
WO (1) | WO2008136884A1 (ru) |
Families Citing this family (36)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2185877B1 (en) * | 2007-08-24 | 2021-01-20 | ExxonMobil Upstream Research Company | Natural gas liquefaction process and system |
AU2009249761B2 (en) * | 2008-05-20 | 2012-10-04 | Shell Internationale Research Maatschappij B.V. | Method of cooling and liquefying a hydrocarbon stream, an apparatus therefor, and a floating structure, caisson or off-shore platform comprising such an apparatus |
GB2469077A (en) * | 2009-03-31 | 2010-10-06 | Dps Bristol | Process for the offshore liquefaction of a natural gas feed |
FR2957140B1 (fr) * | 2010-03-08 | 2014-09-12 | Total Sa | Procede de liquefaction de gaz naturel utilisant de l'azote enrichi en tant que fluide frigorigene |
FR2957141B1 (fr) * | 2010-03-08 | 2012-08-17 | Total Sa | Procede de liquefaction de gaz naturel utilisant un melange co2 / hfc en tant que fluide frigorigene |
WO2012112692A1 (en) * | 2011-02-16 | 2012-08-23 | Conocophillips Company | Integrated waste heat recovery in liquefied natural gas facility |
EP2859290A4 (en) * | 2012-06-06 | 2016-11-30 | Keppel Offshore & Marine Technology Ct Pte Ltd | SYSTEM AND METHOD FOR LIQUEFACTION OF A NATURAL GAS |
US20140157824A1 (en) * | 2012-12-06 | 2014-06-12 | L'air Liquide Societe Anonyme Pour I'etude Et I'exploitation Des Procedes Georges Claude | Method for improved thermal performing refrigeration cycle |
EP2957621A1 (en) | 2014-06-17 | 2015-12-23 | Shell International Research Maatschappij B.V. | De-superheater system and compression system employing such de-superheater system, and method of producing a pressurized and at least partially condensed mixture of hydrocarbons |
EP2957620A1 (en) * | 2014-06-17 | 2015-12-23 | Shell International Research Maatschappij B.V. | Method and system for producing a pressurized and at least partially condensed mixture of hydrocarbons |
SG10202005527RA (en) * | 2015-12-14 | 2020-07-29 | Exxonmobil Upstream Res Co | Pre-cooling of natural gas by high pressure compression and expansion |
US20170191750A1 (en) * | 2015-12-31 | 2017-07-06 | General Electric Company | System and method for compressor intercooler |
CN105737520A (zh) * | 2016-02-25 | 2016-07-06 | 蚌埠市荣强压缩机制造有限公司 | 天然气液化的方法及其专用天然气液化装置 |
KR101792708B1 (ko) * | 2016-06-22 | 2017-11-02 | 삼성중공업(주) | 유체냉각장치 |
EP3309488A1 (en) * | 2016-10-13 | 2018-04-18 | Shell International Research Maatschappij B.V. | System for treating and cooling a hydrocarbon stream |
US20180220552A1 (en) * | 2017-01-31 | 2018-08-02 | Fluor Technologies Corporation | Modular processing facility with distributed cooling systems |
KR102244172B1 (ko) | 2017-02-24 | 2021-04-27 | 엑손모빌 업스트림 리서치 캄파니 | 이중 목적의 액화 천연가스/액화 질소 저장 탱크를 퍼징하는 방법 |
US20190101328A1 (en) | 2017-09-29 | 2019-04-04 | Fritz Pierre, JR. | Natural Gas Liquefaction by a High Pressure Expansion Process |
EP3688390A1 (en) | 2017-09-29 | 2020-08-05 | ExxonMobil Upstream Research Company | Natural gas liquefaction by a high pressure expansion process |
EP3701206A1 (en) | 2017-10-25 | 2020-09-02 | ExxonMobil Upstream Research Company | Natural gas liquefaction by a high pressure expansion process using multiple turboexpander compressors |
WO2019236246A1 (en) | 2018-06-07 | 2019-12-12 | Exxonmobil Upstream Research Company | Pretreatment and pre-cooling of natural gas by high pressure compression and expansion |
SG11202101058QA (en) | 2018-08-22 | 2021-03-30 | Exxonmobil Upstream Res Co | Heat exchanger configuration for a high pressure expander process and a method of natural gas liquefaction using the same |
CA3109918C (en) | 2018-08-22 | 2023-05-16 | Exxonmobil Upstream Research Company | Managing make-up gas composition variation for a high pressure expander process |
WO2020040952A1 (en) | 2018-08-22 | 2020-02-27 | Exxonmobil Upstream Research Company | Primary loop start-up method for a high pressure expander process |
JP2022517930A (ja) | 2019-01-30 | 2022-03-11 | エクソンモービル アップストリーム リサーチ カンパニー | Lng冷媒からの水分除去方法 |
US11668524B2 (en) | 2019-01-30 | 2023-06-06 | Exxonmobil Upstream Research Company | Methods for removal of moisture from LNG refrigerant |
US11465093B2 (en) | 2019-08-19 | 2022-10-11 | Exxonmobil Upstream Research Company | Compliant composite heat exchangers |
US20210063083A1 (en) | 2019-08-29 | 2021-03-04 | Exxonmobil Upstream Research Company | Liquefaction of Production Gas |
JP7326483B2 (ja) | 2019-09-19 | 2023-08-15 | エクソンモービル・テクノロジー・アンド・エンジニアリング・カンパニー | 高圧圧縮及び膨張による天然ガスの前処理及び予冷 |
US11815308B2 (en) | 2019-09-19 | 2023-11-14 | ExxonMobil Technology and Engineering Company | Pretreatment and pre-cooling of natural gas by high pressure compression and expansion |
WO2021055074A1 (en) | 2019-09-20 | 2021-03-25 | Exxonmobil Upstream Research Company | Removal of acid gases from a gas stream, with o2 enrichment for acid gas capture and sequestration |
US11808411B2 (en) | 2019-09-24 | 2023-11-07 | ExxonMobil Technology and Engineering Company | Cargo stripping features for dual-purpose cryogenic tanks on ships or floating storage units for LNG and liquid nitrogen |
WO2022099233A1 (en) | 2020-11-03 | 2022-05-12 | Exxonmobil Upstream Research Company | Natural gas liquefaction methods and systems featuring feed compression, expansion and recycling |
US20220252341A1 (en) * | 2021-02-05 | 2022-08-11 | Air Products And Chemicals, Inc. | Method and system for decarbonized lng production |
US20220333856A1 (en) * | 2021-04-15 | 2022-10-20 | Henry Edward Howard | System and method to produce liquefied natural gas using two distinct refrigeration cycles with an integral gear machine |
US20230272971A1 (en) * | 2022-02-28 | 2023-08-31 | Air Products And Chemicals, Inc, | Single mixed refrigerant lng production process |
Family Cites Families (58)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3162519A (en) | 1958-06-30 | 1964-12-22 | Conch Int Methane Ltd | Liquefaction of natural gas |
US3323315A (en) | 1964-07-15 | 1967-06-06 | Conch Int Methane Ltd | Gas liquefaction employing an evaporating and gas expansion refrigerant cycles |
DE1626325B1 (de) | 1964-11-03 | 1969-10-23 | Linde Ag | Verfahren und Einrichtung zum Verfluessigen von tiefsiedenden Gasen |
DE1501730A1 (de) | 1966-05-27 | 1969-10-30 | Linde Ag | Verfahren und Vorrichtung zum Verfluessigen von Erdgas |
US3407052A (en) | 1966-08-17 | 1968-10-22 | Conch Int Methane Ltd | Natural gas liquefaction with controlled b.t.u. content |
GB1096697A (en) * | 1966-09-27 | 1967-12-29 | Int Research & Dev Co Ltd | Process for liquefying natural gas |
DE2110417A1 (de) | 1971-03-04 | 1972-09-21 | Linde Ag | Verfahren zum Verfluessigen und Unterkuehlen von Erdgas |
JPS6060463A (ja) | 1983-09-14 | 1985-04-08 | 株式会社日立製作所 | 液化ガス発生装置 |
US4740223A (en) | 1986-11-03 | 1988-04-26 | The Boc Group, Inc. | Gas liquefaction method and apparatus |
US4755200A (en) | 1987-02-27 | 1988-07-05 | Air Products And Chemicals, Inc. | Feed gas drier precooling in mixed refrigerant natural gas liquefaction processes |
US5036671A (en) | 1990-02-06 | 1991-08-06 | Liquid Air Engineering Company | Method of liquefying natural gas |
FR2714722B1 (fr) * | 1993-12-30 | 1997-11-21 | Inst Francais Du Petrole | Procédé et appareil de liquéfaction d'un gaz naturel. |
AUPM485694A0 (en) | 1994-04-05 | 1994-04-28 | Bhp Petroleum Pty. Ltd. | Liquefaction process |
US5473900A (en) * | 1994-04-29 | 1995-12-12 | Phillips Petroleum Company | Method and apparatus for liquefaction of natural gas |
DE19517116C1 (de) | 1995-05-10 | 1996-06-20 | Linde Ag | Verfahren zur Verringerung des Energieverbrauchs |
RU2141084C1 (ru) | 1995-10-05 | 1999-11-10 | Би Эйч Пи Петролеум ПТИ. Лтд. | Установка для сжижения |
FR2743140B1 (fr) | 1995-12-28 | 1998-01-23 | Inst Francais Du Petrole | Procede et dispositif de liquefaction en deux etapes d'un melange gazeux tel qu'un gaz naturel |
US5657643A (en) * | 1996-02-28 | 1997-08-19 | The Pritchard Corporation | Closed loop single mixed refrigerant process |
US5669234A (en) | 1996-07-16 | 1997-09-23 | Phillips Petroleum Company | Efficiency improvement of open-cycle cascaded refrigeration process |
US5755114A (en) | 1997-01-06 | 1998-05-26 | Abb Randall Corporation | Use of a turboexpander cycle in liquefied natural gas process |
JPH10204455A (ja) | 1997-01-27 | 1998-08-04 | Chiyoda Corp | 天然ガス液化方法 |
US5836173A (en) | 1997-05-01 | 1998-11-17 | Praxair Technology, Inc. | System for producing cryogenic liquid |
DZ2535A1 (fr) * | 1997-06-20 | 2003-01-08 | Exxon Production Research Co | Procédé perfectionné pour la liquéfaction de gaz naturel. |
US5931021A (en) | 1997-06-24 | 1999-08-03 | Shnaid; Isaac | Straightforward method and once-through apparatus for gas liquefaction |
US5992175A (en) | 1997-12-08 | 1999-11-30 | Ipsi Llc | Enhanced NGL recovery processes |
US6446465B1 (en) | 1997-12-11 | 2002-09-10 | Bhp Petroleum Pty, Ltd. | Liquefaction process and apparatus |
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 |
US5983665A (en) | 1998-03-03 | 1999-11-16 | Air Products And Chemicals, Inc. | Production of refrigerated liquid methane |
FR2778232B1 (fr) | 1998-04-29 | 2000-06-02 | Inst Francais Du Petrole | Procede et dispositif de liquefaction d'un gaz naturel sans separation de phases sur les melanges refrigerants |
US6006545A (en) | 1998-08-14 | 1999-12-28 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes | Liquefier process |
US6269656B1 (en) | 1998-09-18 | 2001-08-07 | Richard P. Johnston | Method and apparatus for producing liquified natural gas |
US6085545A (en) | 1998-09-18 | 2000-07-11 | Johnston; Richard P. | Liquid natural gas system with an integrated engine, compressor and expander assembly |
TW421704B (en) | 1998-11-18 | 2001-02-11 | Shell Internattonale Res Mij B | Plant for liquefying natural gas |
US6119479A (en) | 1998-12-09 | 2000-09-19 | Air Products And Chemicals, Inc. | Dual mixed refrigerant cycle for gas liquefaction |
EP1039750A3 (en) * | 1999-03-26 | 2005-05-25 | Matsushita Electric Industrial Co., Ltd. | Video storage and retrieval apparatus |
US6070429A (en) | 1999-03-30 | 2000-06-06 | Phillips Petroleum Company | Nitrogen rejection system for liquified natural gas |
US6308531B1 (en) | 1999-10-12 | 2001-10-30 | Air Products And Chemicals, Inc. | Hybrid cycle for the production of liquefied natural gas |
MY122625A (en) | 1999-12-17 | 2006-04-29 | Exxonmobil Upstream Res Co | Process for making pressurized liquefied natural gas from pressured natural gas using expansion cooling |
US6220053B1 (en) | 2000-01-10 | 2001-04-24 | Praxair Technology, Inc. | Cryogenic industrial gas liquefaction system |
FR2803851B1 (fr) | 2000-01-19 | 2006-09-29 | Inst Francais Du Petrole | Procede de liquefaction partielle d'un fluide contenant des hydrocarbures tel que du gaz naturel |
GB0006265D0 (en) | 2000-03-15 | 2000-05-03 | Statoil | Natural gas liquefaction process |
US6484533B1 (en) | 2000-11-02 | 2002-11-26 | Air Products And Chemicals, Inc. | Method and apparatus for the production of a liquid cryogen |
US6412302B1 (en) * | 2001-03-06 | 2002-07-02 | Abb Lummus Global, Inc. - Randall Division | LNG production using dual independent expander refrigeration cycles |
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 |
GB0120272D0 (en) | 2001-08-21 | 2001-10-10 | Gasconsult Ltd | Improved process for liquefaction of natural gases |
US6564578B1 (en) | 2002-01-18 | 2003-05-20 | Bp Corporation North America Inc. | Self-refrigerated LNG process |
US6751985B2 (en) | 2002-03-20 | 2004-06-22 | Exxonmobil Upstream Research Company | Process for producing a pressurized liquefied gas product by cooling and expansion of a gas stream in the supercritical state |
FR2841330B1 (fr) | 2002-06-21 | 2005-01-28 | Inst Francais Du Petrole | Liquefaction de gaz naturel avec recyclage de gaz naturel |
US6622519B1 (en) | 2002-08-15 | 2003-09-23 | Velocys, Inc. | Process for cooling a product in a heat exchanger employing microchannels for the flow of refrigerant and product |
US6694774B1 (en) | 2003-02-04 | 2004-02-24 | Praxair Technology, Inc. | Gas liquefaction method using natural gas and mixed gas refrigeration |
US6889523B2 (en) | 2003-03-07 | 2005-05-10 | Elkcorp | LNG production in cryogenic natural gas processing plants |
US6742357B1 (en) | 2003-03-18 | 2004-06-01 | Air Products And Chemicals, Inc. | Integrated multiple-loop refrigeration process for gas liquefaction |
US6722157B1 (en) | 2003-03-20 | 2004-04-20 | Conocophillips Company | Non-volatile natural gas liquefaction system |
US7127914B2 (en) * | 2003-09-17 | 2006-10-31 | Air Products And Chemicals, Inc. | Hybrid gas liquefaction cycle with multiple expanders |
US7204100B2 (en) | 2004-05-04 | 2007-04-17 | Ortloff Engineers, Ltd. | Natural gas liquefaction |
US7228714B2 (en) * | 2004-10-28 | 2007-06-12 | Praxair Technology, Inc. | Natural gas liquefaction system |
JP5139292B2 (ja) * | 2005-08-09 | 2013-02-06 | エクソンモービル アップストリーム リサーチ カンパニー | Lngのための天然ガス液化方法 |
-
2008
- 2008-03-04 US US12/527,539 patent/US8616021B2/en active Active
- 2008-03-04 CA CA2681417A patent/CA2681417C/en active Active
- 2008-03-04 AU AU2008246345A patent/AU2008246345B2/en active Active
- 2008-03-04 RU RU2009144777/06A patent/RU2458296C2/ru not_active IP Right Cessation
- 2008-03-04 WO PCT/US2008/002861 patent/WO2008136884A1/en active Application Filing
- 2008-03-04 BR BRPI0808909-4A patent/BRPI0808909A2/pt not_active IP Right Cessation
-
2009
- 2009-12-02 NO NO20093458A patent/NO20093458L/no not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
RU2458296C2 (ru) | 2012-08-10 |
US20100107684A1 (en) | 2010-05-06 |
US8616021B2 (en) | 2013-12-31 |
AU2008246345B2 (en) | 2011-12-22 |
CA2681417A1 (en) | 2008-11-13 |
CA2681417C (en) | 2016-07-26 |
WO2008136884A1 (en) | 2008-11-13 |
NO20093458L (no) | 2010-01-29 |
BRPI0808909A2 (pt) | 2014-08-19 |
AU2008246345A1 (en) | 2008-11-13 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
RU2009144777A (ru) | Способ сжижения природного газа | |
TWI379986B (en) | System to cold compress an air stream using natural gas refrigeration | |
RU2008108998A (ru) | Способ ожижения природного газа для получения сжиженного природного газа | |
RU2011124891A (ru) | Способ и система сжижения | |
JP2010537151A5 (ru) | ||
JP2016505793A5 (ru) | ||
RU2006112569A (ru) | Комбинированный цикл сжижения газа, использующий множество детандеров | |
RU2007122345A (ru) | Способ криогенного сжижения/охлаждения и система для осуществления способа | |
MY152657A (en) | Method for processing a stream or lng obtained by means of cooling using a first refrigeration cycle and associated installation | |
WO2017121042A1 (zh) | 一种膨胀制冷富甲烷气液化的方法及装置 | |
KR101669729B1 (ko) | Lng냉열이용 팽창기체 흡입식 공기액화장치 | |
US20110113825A1 (en) | Dual nitrogen expansion process | |
MY176671A (en) | System and method for liquefaction of natural gas | |
MY174100A (en) | System and integrated process for liquid natural gas production | |
RU2015135574A (ru) | Производство сжиженного природного газа | |
RU2013116391A (ru) | Сжижение природного газа с удалением исходной воды | |
RU2013105777A (ru) | Энергосберегающее получение со2 с использованием одноступенчатого расширения и насосов для усиленного испарения | |
PE20040921A1 (es) | Disposicion de licuefaccion de gas natural no volatil | |
RU2018106658A (ru) | Способ получения сжиженного природного газа | |
FI2920526T3 (fi) | Parannuksia jäähdytykseen | |
RU2018124786A (ru) | Судно, содержащее двигатель | |
RU2001122814A (ru) | Способ производства богатой метаном жидкости | |
RU2017110050A (ru) | Сдвоенная система со смешанным хладагентом | |
JP5866193B2 (ja) | 高圧窒素を製造するための方法および装置 | |
RU2017110052A (ru) | Сдвоенная система со смешанным хладагентом |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
MM4A | The patent is invalid due to non-payment of fees |
Effective date: 20180305 |