GB996929A - Improvements in or relating to preparation of liquefied natural hydrocarbon gas - Google Patents
Improvements in or relating to preparation of liquefied natural hydrocarbon gasInfo
- Publication number
- GB996929A GB996929A GB12766/63A GB1276663A GB996929A GB 996929 A GB996929 A GB 996929A GB 12766/63 A GB12766/63 A GB 12766/63A GB 1276663 A GB1276663 A GB 1276663A GB 996929 A GB996929 A GB 996929A
- Authority
- GB
- United Kingdom
- Prior art keywords
- line
- liquid
- gas
- fraction
- exchangers
- 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
Links
- 229930195733 hydrocarbon Natural products 0.000 title abstract 4
- 150000002430 hydrocarbons Chemical class 0.000 title abstract 4
- 239000004215 Carbon black (E152) Substances 0.000 title abstract 3
- 239000007788 liquid Substances 0.000 abstract 10
- 239000007789 gas Substances 0.000 abstract 6
- 239000011261 inert gas Substances 0.000 abstract 4
- 239000000567 combustion gas Substances 0.000 abstract 3
- 239000000203 mixture Substances 0.000 abstract 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract 2
- 238000001816 cooling Methods 0.000 abstract 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract 2
- 229910002092 carbon dioxide Inorganic materials 0.000 abstract 1
- 239000001569 carbon dioxide Substances 0.000 abstract 1
- 239000001307 helium Substances 0.000 abstract 1
- 229910052734 helium Inorganic materials 0.000 abstract 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 239000002808 molecular sieve Substances 0.000 abstract 1
- 229910052757 nitrogen Inorganic materials 0.000 abstract 1
- 239000003507 refrigerant Substances 0.000 abstract 1
- 238000000926 separation method Methods 0.000 abstract 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 abstract 1
Classifications
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- 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
- F25J1/0085—Ethane; Ethylene
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- 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
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- 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
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- 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"
- F25J1/0045—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 vaporising a liquid return stream
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- F25J1/0207—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 single-component refrigerant [SCR] fluid in a closed vapor compression cycle as at least a three level SCR refrigeration cascade
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- 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
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- 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
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- 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
- F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
- F25J2290/62—Details of storing a fluid in a tank
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
996,929. Cold separation of gas mixtures. SOC. D'ETUDES DU TRANSPORT ET DE LA VALORISATION DES GAZ NATURELS DU SARAHA S.E.G.A.N.S. April 1, 1963 [April 5, 1962], No. 12766/63. Heading F4P. A process for separating a liquefied natural hydrocarbon gas mixture containing volatile inert gases such as nitrogen and helium into a sub-cooled liquid fraction and into a gaseous combustible fraction comprises expanding feed liquid from lines 1, 2, Fig. 1, into a flask B 1 , withdrawing the liquid fraction so produced through a line 3 and sub-cooling it in exchangers E 2 , E 3 arranged in cascade, withdrawing the combustible gaseous fraction through a line 6 and partially condensing it in exchangers E 5 , E 6 also arranged in cascade followed by further cooling the product liquid fraction and liquefying the combustible fraction in exchangers E 4 , E 7 cooled by a return flow of liquid combustion gas after expansion at a valve in a line 8; product liquid fraction being withdrawn through a line 5 and product combustion gas containing inert gas being withdrawn through a line 9. As shown, liquid feed in line 1 is sub-cooled in an exchanger E 1 which forms the high pressure stage of a threestage methane refrigerant cycle, the medium and low pressure stages of which comprise exchangers E 2 , E 5 and E 3 , E 6 respectively. The inert volatile gas content of the liquid hydrocarbon product may be reduced by substituting a column V 1 , Fig. 4, in place of the flask B 1 and inert gases are separated from the combustible gas in line 6 by means of a separating column V 2 from which liquefied combustible gas is withdrawn through a line 10 and after being sub-cooled in cascade exchanger E 6 and in exchangers E 7a , E 7b in counterflow to expanded gas the latter is discharged as product through line 9. A portion of liquid combustion gas leaving exchanger E 7b through line 8 is diverted along a line 11 and cools the head of column V 2 from which inert gases are withdrawn through a line 13 and are passed through a molecular sieve 14. The carbon-dioxide content of the mixture of liquid hydrocarbons withdrawn from the base of column V 1 through line 3 and having been sub-cooled in exchanger E 2 is removed by expansion into flasks B 3 , B 4 , Fig. 6 (not shown) having filter screens therein.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR893475A FR1331960A (en) | 1962-04-05 | 1962-04-05 | Natural gas liquefaction process |
Publications (1)
Publication Number | Publication Date |
---|---|
GB996929A true GB996929A (en) | 1965-06-30 |
Family
ID=8776187
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB12766/63A Expired GB996929A (en) | 1962-04-05 | 1963-04-01 | Improvements in or relating to preparation of liquefied natural hydrocarbon gas |
Country Status (7)
Country | Link |
---|---|
US (1) | US3254496A (en) |
BE (1) | BE630256A (en) |
DE (1) | DE1267236B (en) |
FR (1) | FR1331960A (en) |
GB (1) | GB996929A (en) |
LU (1) | LU43449A1 (en) |
NL (1) | NL291145A (en) |
Families Citing this family (30)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1011453A (en) * | 1964-01-23 | 1965-12-01 | Conch Int Methane Ltd | Process for liquefying natural gas |
GB1038535A (en) * | 1964-03-10 | 1966-08-10 | British Oxygen Co Ltd | Process and apparatus for the removal of one or more constituents from a gas mixture |
GB997808A (en) * | 1964-06-17 | 1965-07-07 | Couch Internat Methane Ltd | Cold separation of gas mixtures |
US3340699A (en) * | 1965-06-11 | 1967-09-12 | Little Inc A | Cryogenic condenser with liquid level sensing and control |
US3407614A (en) * | 1966-12-19 | 1968-10-29 | Phillips Petroleum Co | Helium purification |
GB1208196A (en) * | 1967-12-20 | 1970-10-07 | Messer Griesheim Gmbh | Process for the liquifaction of nitrogen-containing natural gas |
JPS4945053B1 (en) * | 1969-02-28 | 1974-12-02 | ||
US3653220A (en) * | 1969-05-09 | 1972-04-04 | Airco Boc Cryogenic Plants Cor | Process for helium recovery and purification |
US3815376A (en) * | 1969-07-31 | 1974-06-11 | Airco Inc | Process and system for the production and purification of helium |
US4032337A (en) * | 1976-07-27 | 1977-06-28 | Crucible Inc. | Method and apparatus for pressurizing hot-isostatic pressure vessels |
GB2139548B (en) * | 1983-05-11 | 1986-11-19 | James Watson Hendry | Injection moulding |
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 |
US7594414B2 (en) * | 2001-05-04 | 2009-09-29 | Battelle Energy Alliance, Llc | Apparatus for the liquefaction of natural gas and methods relating to same |
US20070107465A1 (en) * | 2001-05-04 | 2007-05-17 | Battelle Energy Alliance, Llc | Apparatus for the liquefaction of 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 |
US7637122B2 (en) * | 2001-05-04 | 2009-12-29 | Battelle Energy Alliance, Llc | Apparatus for the liquefaction of a 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 |
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 |
US8555672B2 (en) * | 2009-10-22 | 2013-10-15 | Battelle Energy Alliance, Llc | Complete liquefaction methods and apparatus |
US8061413B2 (en) | 2007-09-13 | 2011-11-22 | Battelle Energy Alliance, Llc | Heat exchangers comprising at least one porous member positioned within a casing |
US9217603B2 (en) | 2007-09-13 | 2015-12-22 | Battelle Energy Alliance, Llc | Heat exchanger and related methods |
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 |
US20110094261A1 (en) * | 2009-10-22 | 2011-04-28 | Battelle Energy Alliance, Llc | Natural gas liquefaction core modules, plants including same and related methods |
US10655911B2 (en) | 2012-06-20 | 2020-05-19 | Battelle Energy Alliance, Llc | Natural gas liquefaction employing independent refrigerant path |
US20140366577A1 (en) | 2013-06-18 | 2014-12-18 | Pioneer Energy Inc. | Systems and methods for separating alkane gases with applications to raw natural gas processing and flare gas capture |
US20160109177A1 (en) | 2014-10-16 | 2016-04-21 | General Electric Company | System and method for natural gas liquefaction |
RU2615862C2 (en) * | 2015-05-19 | 2017-04-11 | Ооо "Зиф" | Small-size natural gas liquefaction unit |
IT201700103870A1 (en) * | 2017-09-18 | 2019-03-18 | Criotec Impianti S P A | Plant and procedure for biogas upgrading. |
FR3127557B1 (en) | 2021-09-28 | 2024-01-26 | Cryo Pur | Process for icing carbon dioxide contained in liquid methane |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL24285C (en) * | 1927-01-24 | |||
DE620077C (en) * | 1934-03-23 | 1935-10-14 | Linde Eismasch Ag | Process for the separation of gas mixtures |
US2386297A (en) * | 1943-10-07 | 1945-10-09 | Air Reduction | Separation of the constituents of gaseous mixtures by liquefaction and rectification |
US2557171A (en) * | 1946-11-12 | 1951-06-19 | Pritchard & Co J F | Method of treating natural gas |
US2582148A (en) * | 1947-05-15 | 1952-01-08 | Pritchard & Co J F | Method of recovering desirable liquefiable hydrocarbons |
US2679145A (en) * | 1951-12-08 | 1954-05-25 | Union Stock Yards & Transit Co | Regenerative method and apparatus for liquefying natural gas |
US3162519A (en) * | 1958-06-30 | 1964-12-22 | Conch Int Methane Ltd | Liquefaction of natural gas |
US2960837A (en) * | 1958-07-16 | 1960-11-22 | Conch Int Methane Ltd | Liquefying natural gas with low pressure refrigerants |
US2940271A (en) * | 1959-03-24 | 1960-06-14 | Fluor Corp | Low temperature fractionation of natural gas components |
US3057167A (en) * | 1959-10-12 | 1962-10-09 | Union Carbide Corp | Process and apparatus for separating helium from helium-air mixtures |
US3026682A (en) * | 1960-01-27 | 1962-03-27 | Kellogg M W Co | Separation of hydrogen and methane |
-
0
- BE BE630256D patent/BE630256A/xx unknown
- NL NL291145D patent/NL291145A/xx unknown
-
1962
- 1962-04-05 FR FR893475A patent/FR1331960A/en not_active Expired
-
1963
- 1963-03-29 LU LU43449D patent/LU43449A1/xx unknown
- 1963-04-01 GB GB12766/63A patent/GB996929A/en not_active Expired
- 1963-04-02 US US270109A patent/US3254496A/en not_active Expired - Lifetime
- 1963-04-04 DE DEP1267A patent/DE1267236B/en active Pending
Also Published As
Publication number | Publication date |
---|---|
NL291145A (en) | |
FR1331960A (en) | 1963-07-12 |
DE1267236B (en) | 1968-05-02 |
LU43449A1 (en) | 1963-05-29 |
US3254496A (en) | 1966-06-07 |
BE630256A (en) |
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