GB1315003A - Gas mixture rectification - Google Patents
Gas mixture rectificationInfo
- Publication number
- GB1315003A GB1315003A GB2142470A GB2142470A GB1315003A GB 1315003 A GB1315003 A GB 1315003A GB 2142470 A GB2142470 A GB 2142470A GB 2142470 A GB2142470 A GB 2142470A GB 1315003 A GB1315003 A GB 1315003A
- Authority
- GB
- United Kingdom
- Prior art keywords
- withdrawn
- column
- oxygen
- condenser
- product
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/143—Fractional distillation or use of a fractionation or rectification column by two or more of a fractionation, separation or rectification 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
- 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
- F25J3/04406—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 a dual pressure main column system
- F25J3/04412—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 a dual pressure main column system in a classical double column flowsheet, i.e. with thermal coupling by a main reboiler-condenser in the bottom of low pressure respectively top of high pressure 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
- 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
- F25J3/04642—Recovering noble gases from air
- F25J3/04648—Recovering noble gases from air argon
- F25J3/04654—Producing crude argon in a crude argon column
- F25J3/04666—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system
- F25J3/04672—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system having a top condenser
-
- 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
- F25J3/04642—Recovering noble gases from air
- F25J3/04648—Recovering noble gases from air argon
- F25J3/04654—Producing crude argon in a crude argon column
- F25J3/04666—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system
- F25J3/04672—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system having a top condenser
- F25J3/04678—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system having a top condenser cooled by oxygen enriched liquid from high pressure column bottoms
-
- 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
- F25J3/04642—Recovering noble gases from air
- F25J3/04648—Recovering noble gases from air argon
- F25J3/04654—Producing crude argon in a crude argon column
- F25J3/04666—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system
- F25J3/04672—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system having a top condenser
- F25J3/04684—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system having a top condenser and a bottom re-boiler
-
- 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
- Y10S62/923—Inert gas
- Y10S62/924—Argon
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)
- Separation By Low-Temperature Treatments (AREA)
Abstract
1315003 Separation of argon from air L'AIR LIQUIDE SOC ANON POUR L'ETUDE ET L'EXPLOITATION DES PROCEDES GEORGES CLAUDE 4 May 1970 [5 May 1969] 21424/70 Heading F4P In a three component gas mixture rectification process for the production of a component present in small proportion and of boiling point intermediate those of the remaining two components, e.g. argon, oxygen and nitrogen respectively a gaseous fraction is withdrawn at an intermediate level 8 from the low pressure stage 2 of a double column 1, 2 passed to an auxiliary rectification column 4 where it is in part condensed by vaporization in a condenser 7 of a liquid fraction withdrawn from the main column and the condensate is returned at 9 to said intermediate level. As shown cooling of condenser 7 is effected by a liquid oxygen fraction withdrawn from the: column 2 through a line 14 and the so-vaporized oxygen is withdrawn as product at 114. Reflux for column 4 is provided by a condenser 6 cooled by crude liquid oxygen, and product argon-rid gas is withdrawn at 11. In a modification condenser (7), Fig. 2 (not shown), is cooled by liquid nitrogen withdrawn from the top of column 1 thereby obtaining product gaseous nitrogen; product oxygen being withdrawn from column (2) through line (14).
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR6914244A FR2041701B1 (en) | 1969-05-05 | 1969-05-05 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1315003A true GB1315003A (en) | 1973-04-26 |
Family
ID=9033486
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2142470A Expired GB1315003A (en) | 1969-05-05 | 1970-05-04 | Gas mixture rectification |
Country Status (8)
Country | Link |
---|---|
US (1) | US3729943A (en) |
JP (1) | JPS5617584B1 (en) |
BE (1) | BE749882A (en) |
DE (1) | DE2021140B2 (en) |
ES (1) | ES379208A1 (en) |
FR (1) | FR2041701B1 (en) |
GB (1) | GB1315003A (en) |
LU (1) | LU60844A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4783208A (en) * | 1986-11-24 | 1988-11-08 | The Boc Group Plc | Air separation |
Families Citing this family (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3983711A (en) * | 1975-01-02 | 1976-10-05 | The Lummus Company | Plural stage distillation of a natural gas stream |
US4433990A (en) | 1981-12-08 | 1984-02-28 | Union Carbide Corporation | Process to recover argon from oxygen-only air separation plant |
US4670031A (en) * | 1985-04-29 | 1987-06-02 | Erickson Donald C | Increased argon recovery from air distillation |
US4715874A (en) * | 1986-09-08 | 1987-12-29 | Erickson Donald C | Retrofittable argon recovery improvement to air separation |
EP0269342B1 (en) * | 1986-11-24 | 1991-06-12 | The BOC Group plc | Air separation |
EP0286314B1 (en) * | 1987-04-07 | 1992-05-20 | The BOC Group plc | Air separation |
US4775399A (en) * | 1987-11-17 | 1988-10-04 | Erickson Donald C | Air fractionation improvements for nitrogen production |
US4871382A (en) * | 1987-12-14 | 1989-10-03 | Air Products And Chemicals, Inc. | Air separation process using packed columns for oxygen and argon recovery |
USRE34038E (en) * | 1987-12-14 | 1992-08-25 | Air Products And Chemicals, Inc. | Separating argon/oxygen mixtures using a structured packing |
US4836836A (en) * | 1987-12-14 | 1989-06-06 | Air Products And Chemicals, Inc. | Separating argon/oxygen mixtures using a structured packing |
US4838913A (en) * | 1988-02-10 | 1989-06-13 | Union Carbide Corporation | Double column air separation process with hybrid upper column |
US4842625A (en) * | 1988-04-29 | 1989-06-27 | Air Products And Chemicals, Inc. | Control method to maximize argon recovery from cryogenic air separation units |
US4838785A (en) * | 1988-07-05 | 1989-06-13 | Cameron Forge Company | Walking beam furnace insulation |
CN1025067C (en) * | 1989-02-23 | 1994-06-15 | 琳德股份公司 | Process and method of seperating air by rectification |
FR2650378A1 (en) * | 1989-07-28 | 1991-02-01 | Air Liquide | AIR DISTILLATION SYSTEM PRODUCING ARGON |
US4994098A (en) * | 1990-02-02 | 1991-02-19 | Air Products And Chemicals, Inc. | Production of oxygen-lean argon from air |
US5799508A (en) * | 1996-03-21 | 1998-09-01 | Praxair Technology, Inc. | Cryogenic air separation system with split kettle liquid |
US20030000248A1 (en) * | 2001-06-18 | 2003-01-02 | Brostow Adam Adrian | Medium-pressure nitrogen production with high oxygen recovery |
CA3063409A1 (en) | 2017-05-16 | 2018-11-22 | Terrence J. Ebert | Apparatus and process for liquefying gases |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3127260A (en) * | 1964-03-31 | Separation of air into nitrogen | ||
NL30531C (en) * | 1930-02-07 | |||
NL68365C (en) * | 1947-10-22 | 1900-01-01 | ||
FR980658A (en) * | 1948-02-12 | 1951-05-16 | British Oxygen Co Ltd | Fractional air separation process |
US2559132A (en) * | 1948-02-12 | 1951-07-03 | British Oxygen Co Ltd | Fractional separation of air |
DE1854836U (en) * | 1958-05-20 | 1962-07-12 | Union Carbide Corp | DEVICE FOR SEPARATING AIR AT LOW TEMPERATURE. |
GB929798A (en) * | 1960-04-11 | 1963-06-26 | British Oxygen Co Ltd | Low temperature separation of air |
DE1112997B (en) * | 1960-08-13 | 1961-08-24 | Linde Eismasch Ag | Process and device for gas separation by rectification at low temperature |
US3079759A (en) * | 1961-03-22 | 1963-03-05 | Air Prod & Chem | Separation of gaseous mixtures |
DE1501722A1 (en) * | 1966-01-13 | 1969-06-26 | Linde Ag | Process for cryogenic air separation for the production of highly compressed gaseous and / or liquid oxygen |
GB1180904A (en) * | 1966-06-01 | 1970-02-11 | British Oxygen Co Ltd | Air Separation Process. |
-
1969
- 1969-05-05 FR FR6914244A patent/FR2041701B1/fr not_active Expired
-
1970
- 1970-04-28 US US00032613A patent/US3729943A/en not_active Expired - Lifetime
- 1970-04-30 DE DE2021140A patent/DE2021140B2/en not_active Ceased
- 1970-04-30 ES ES379208A patent/ES379208A1/en not_active Expired
- 1970-05-04 LU LU60844D patent/LU60844A1/xx unknown
- 1970-05-04 BE BE749882D patent/BE749882A/en not_active IP Right Cessation
- 1970-05-04 JP JP3760370A patent/JPS5617584B1/ja active Pending
- 1970-05-04 GB GB2142470A patent/GB1315003A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4783208A (en) * | 1986-11-24 | 1988-11-08 | The Boc Group Plc | Air separation |
Also Published As
Publication number | Publication date |
---|---|
US3729943A (en) | 1973-05-01 |
DE2021140A1 (en) | 1970-11-19 |
DE2021140B2 (en) | 1980-03-20 |
FR2041701A1 (en) | 1971-02-05 |
ES379208A1 (en) | 1973-02-01 |
FR2041701B1 (en) | 1974-02-01 |
LU60844A1 (en) | 1970-07-07 |
JPS5617584B1 (en) | 1981-04-23 |
BE749882A (en) | 1970-11-04 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed [section 19, patents act 1949] | ||
PE20 | Patent expired after termination of 20 years |