GB890458A - Low temperature separation of gas mixtures - Google Patents
Low temperature separation of gas mixturesInfo
- Publication number
- GB890458A GB890458A GB42413/59A GB4241359A GB890458A GB 890458 A GB890458 A GB 890458A GB 42413/59 A GB42413/59 A GB 42413/59A GB 4241359 A GB4241359 A GB 4241359A GB 890458 A GB890458 A GB 890458A
- Authority
- GB
- United Kingdom
- Prior art keywords
- nitrogen
- oxygen
- gas
- exchanger
- container
- 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
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
- 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
- F25J3/04—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 for air
- F25J3/04248—Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion
- F25J3/04333—Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using quasi-closed loop internal vapor compression refrigeration cycles, e.g. of intermediate or oxygen enriched (waste-)streams
- F25J3/04351—Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using quasi-closed loop internal vapor compression refrigeration cycles, e.g. of intermediate or oxygen enriched (waste-)streams 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
- 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
- F25J3/04—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 for air
- F25J3/04006—Providing pressurised feed air or process streams within or from the air fractionation unit
- F25J3/04078—Providing pressurised feed air or process streams within or from the air fractionation unit providing pressurized products by liquid compression and vaporisation with cold recovery, i.e. so-called internal compression
- F25J3/0409—Providing pressurised feed air or process streams within or from the air fractionation unit providing pressurized products by liquid compression and vaporisation with cold recovery, i.e. so-called internal compression of oxygen
-
- 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
- F25J3/04—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 for air
- F25J3/04151—Purification and (pre-)cooling of the feed air; recuperative heat-exchange with product streams
- F25J3/04187—Cooling of the purified feed air by recuperative heat-exchange; Heat-exchange with product streams
- F25J3/04218—Parallel arrangement of the main heat exchange line in cores having different functions, e.g. in low pressure and high pressure cores
- F25J3/04224—Cores associated with a liquefaction or refrigeration 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
- 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
- F25J3/04—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 for air
- F25J3/04472—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 for air using the cold from cryogenic liquids produced within the air fractionation unit and stored in internal or intermediate storages
- F25J3/04496—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 for air using the cold from cryogenic liquids produced within the air fractionation unit and stored in internal or intermediate storages for compensating variable air feed or variable product demand by alternating between periods of liquid storage and liquid assist
- F25J3/04503—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 for air using the cold from cryogenic liquids produced within the air fractionation unit and stored in internal or intermediate storages for compensating variable air feed or variable product demand by alternating between periods of liquid storage and liquid assist by exchanging "cold" between at least two different cryogenic liquids, e.g. independently from the main heat exchange line of the air fractionation and/or by using external alternating storage systems
-
- 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
-
- 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
- F25J2250/00—Details related to the use of reboiler-condensers
- F25J2250/30—External or auxiliary boiler-condenser in general, e.g. without a specified fluid or one fluid is not a primary air component or an intermediate fluid
- F25J2250/42—One fluid being 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
- F25J2250/00—Details related to the use of reboiler-condensers
- F25J2250/30—External or auxiliary boiler-condenser in general, e.g. without a specified fluid or one fluid is not a primary air component or an intermediate fluid
- F25J2250/50—One fluid being oxygen
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S62/00—Refrigeration
- Y10S62/912—External refrigeration system
- Y10S62/913—Liquified gas
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Emergency Medicine (AREA)
- Separation By Low-Temperature Treatments (AREA)
Abstract
890,458. Cold separation of gas mixtures. BRITISH OXYGEN CO. Ltd. Dec. 14, 1960 [Dec. 14, 1959], No. 42413/59. Class 8(2). A low temperature gas mixture e.g., air separating plant 1 is continuously operated to satisfy a fluctuating demand for gaseous oxygen discharged through a duct 2 by condensing the excess oxygen gas during a low demand period in an exchanger 5 cooled by an auxiliary liquefied gas of lower boiling point e.g., separated nitrogen stored in a container 6, storing the condensed oxygen in a container 9 and revaporizing it during a high demand period in an exchanger 12 warmed by nitrogen gas withdrawn from the plant 1 and compressed at 15 to a pressure above that at which liquid nitrogen is vaporized in exchanger 5 during a low demand period and feeding nitrogen condensed in the oxygen revaporizor 12 after expansion at a valve 16 and separation in a chamber 17 to the liquid nitrogen container 6. The cold content of the flashed nitrogen in chamber 17 is used to condense nitrogen withdrawn from the inlet side of the compressor 15.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB42413/59A GB890458A (en) | 1959-12-14 | 1959-12-14 | Low temperature separation of gas mixtures |
DEB60462A DE1186478B (en) | 1959-12-14 | 1960-12-12 | Process for the removal of a gaseous separation product from a cryogenic gas mixture separation plant |
FR846695A FR1275951A (en) | 1959-12-14 | 1960-12-12 | Low-temperature separation process for gas mixtures |
US75580A US3058315A (en) | 1959-12-14 | 1960-12-13 | Process for supplying a gaseous product to meet a fluctuating demand |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB42413/59A GB890458A (en) | 1959-12-14 | 1959-12-14 | Low temperature separation of gas mixtures |
Publications (1)
Publication Number | Publication Date |
---|---|
GB890458A true GB890458A (en) | 1962-02-28 |
Family
ID=10424302
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB42413/59A Expired GB890458A (en) | 1959-12-14 | 1959-12-14 | Low temperature separation of gas mixtures |
Country Status (3)
Country | Link |
---|---|
US (1) | US3058315A (en) |
DE (1) | DE1186478B (en) |
GB (1) | GB890458A (en) |
Families Citing this family (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3273349A (en) * | 1965-02-15 | 1966-09-20 | Air Reduction | Variable demand air rectification plant with recycle |
US3271967A (en) * | 1965-02-19 | 1966-09-13 | Phillips Petroleum Co | Fluid handling |
NL131575C (en) * | 1965-04-30 | |||
FR1479561A (en) * | 1966-03-25 | 1967-05-05 | Air Liquide | Variable flow rate gas pre-production process |
DE2139586C2 (en) * | 1971-08-06 | 1973-05-03 | Linde Ag | Process and system for liquefying and re-evaporation of natural gas or methane |
GB1530785A (en) * | 1975-08-07 | 1978-11-01 | British Steel Corp | Scrap treatment |
US4627243A (en) * | 1985-09-26 | 1986-12-09 | Union Carbide Corporation | Gas supply system for variable demand application |
US5060480A (en) * | 1990-10-30 | 1991-10-29 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Process and apparatus for the liquefaction of a flow of gaseous oxygen |
US5152149A (en) * | 1991-07-23 | 1992-10-06 | The Boc Group, Inc. | Air separation method for supplying gaseous oxygen in accordance with a variable demand pattern |
CN1071444C (en) * | 1992-02-21 | 2001-09-19 | 普拉塞尔技术有限公司 | Cryogenic air separation system for producing gaseous oxygen |
FR2704632B1 (en) * | 1993-04-29 | 1995-06-23 | Air Liquide | PROCESS AND PLANT FOR SEPARATING AIR. |
DE19526785C1 (en) * | 1995-07-21 | 1997-02-20 | Linde Ag | Method and device for the variable production of a gaseous printed product |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB699429A (en) * | 1951-08-27 | 1953-11-04 | British Oxygen Co Ltd | Improvements in or relating to the dispensing of gases |
US2685181A (en) * | 1952-04-30 | 1954-08-03 | Emily C Schlitt | Separation of the constituents of gaseous mixtures |
BE525287A (en) * | 1953-03-24 | 1900-01-01 | ||
GB798584A (en) * | 1956-12-18 | 1958-07-23 | Union Carbide Corp | Process and apparatus for separating gas mixtures |
LU35763A1 (en) * | 1957-02-13 | |||
DE1103947B (en) * | 1959-09-11 | 1961-04-06 | Linde Eismasch Ag | Process and device for gas separation in the event of large load fluctuations |
-
1959
- 1959-12-14 GB GB42413/59A patent/GB890458A/en not_active Expired
-
1960
- 1960-12-12 DE DEB60462A patent/DE1186478B/en active Pending
- 1960-12-13 US US75580A patent/US3058315A/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
US3058315A (en) | 1962-10-16 |
DE1186478B (en) | 1965-02-04 |
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