NO155828B - Fremgangsmaate for separering av luft ved rektifisering. - Google Patents
Fremgangsmaate for separering av luft ved rektifisering. Download PDFInfo
- Publication number
- NO155828B NO155828B NO824149A NO824149A NO155828B NO 155828 B NO155828 B NO 155828B NO 824149 A NO824149 A NO 824149A NO 824149 A NO824149 A NO 824149A NO 155828 B NO155828 B NO 155828B
- Authority
- NO
- Norway
- Prior art keywords
- stream
- air
- pressure column
- column
- flow
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 31
- 238000000926 separation method Methods 0.000 title description 25
- 238000001816 cooling Methods 0.000 claims description 16
- 238000010438 heat treatment Methods 0.000 claims description 10
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 30
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 20
- 239000007788 liquid Substances 0.000 description 18
- 229910052757 nitrogen Inorganic materials 0.000 description 15
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 13
- 239000001301 oxygen Substances 0.000 description 13
- 229910052760 oxygen Inorganic materials 0.000 description 13
- 229910052786 argon Inorganic materials 0.000 description 10
- 238000004821 distillation Methods 0.000 description 10
- 239000000356 contaminant Substances 0.000 description 7
- 239000002826 coolant Substances 0.000 description 7
- 238000010992 reflux Methods 0.000 description 7
- 239000000203 mixture Substances 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 5
- 239000002699 waste material Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 230000002411 adverse Effects 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 238000005201 scrubbing Methods 0.000 description 2
- 239000012808 vapor phase Substances 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- OLBVUFHMDRJKTK-UHFFFAOYSA-N [N].[O] Chemical compound [N].[O] OLBVUFHMDRJKTK-UHFFFAOYSA-N 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000005094 computer simulation Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001944 continuous distillation Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 235000003642 hunger Nutrition 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 238000011027 product recovery Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- SRVJKTDHMYAMHA-WUXMJOGZSA-N thioacetazone Chemical compound CC(=O)NC1=CC=C(\C=N\NC(N)=S)C=C1 SRVJKTDHMYAMHA-WUXMJOGZSA-N 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 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
- 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
-
- 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
- F25J3/04284—Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using internal refrigeration by open-loop gas work expansion, e.g. of intermediate or oxygen enriched (waste-)streams
- F25J3/0429—Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using internal refrigeration by open-loop gas work expansion, e.g. of intermediate or oxygen enriched (waste-)streams of feed air, e.g. used as waste or product air or expanded into an auxiliary column
- F25J3/04303—Lachmann expansion, i.e. expanded into oxygen producing or low 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
- F25J3/04151—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
- F25J3/04193—Division of the main heat exchange line in consecutive sections having different functions
-
- 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
- F25J3/04284—Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using internal refrigeration by open-loop gas work expansion, e.g. of intermediate or oxygen enriched (waste-)streams
-
- 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
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/50—Processes or apparatus using separation by rectification using multiple (re-)boiler-condensers at different heights of the column
- F25J2200/52—Processes or apparatus using separation by rectification using multiple (re-)boiler-condensers at different heights of the column in the high pressure column of a double pressure main column system
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/90—Details relating to column internals, e.g. structured packing, gas or liquid distribution
-
- 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
- F25J2205/24—Processes or apparatus using other separation and/or other processing means using regenerators, cold accumulators or reversible heat exchangers
-
- 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
- F25J2205/60—Processes or apparatus using other separation and/or other processing means using adsorption on solid adsorbents, e.g. by temperature-swing adsorption [TSA] at the hot or cold end
-
- 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
- F25J2245/00—Processes or apparatus involving steps for recycling of process streams
- F25J2245/40—Processes or apparatus involving steps for recycling of process streams the recycled stream being air
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Drying Of Gases (AREA)
- Chimneys And Flues (AREA)
- Compressor (AREA)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US06/328,817 US4407135A (en) | 1981-12-09 | 1981-12-09 | Air separation process with turbine exhaust desuperheat |
Publications (2)
Publication Number | Publication Date |
---|---|
NO824149L NO824149L (no) | 1983-06-10 |
NO155828B true NO155828B (no) | 1987-02-23 |
Family
ID=23282572
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
NO824149A NO155828B (no) | 1981-12-09 | 1982-12-09 | Fremgangsmaate for separering av luft ved rektifisering. |
Country Status (14)
Country | Link |
---|---|
US (1) | US4407135A (ja) |
EP (1) | EP0081473B2 (ja) |
JP (1) | JPS58106377A (ja) |
KR (1) | KR880001511B1 (ja) |
AT (1) | ATE31809T1 (ja) |
AU (1) | AU548184B2 (ja) |
BR (1) | BR8207103A (ja) |
CA (1) | CA1173737A (ja) |
DE (1) | DE3277931D1 (ja) |
DK (1) | DK547282A (ja) |
ES (1) | ES518026A0 (ja) |
MX (1) | MX156853A (ja) |
NO (1) | NO155828B (ja) |
ZA (1) | ZA829072B (ja) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6060485A (ja) * | 1983-09-12 | 1985-04-08 | 株式会社神戸製鋼所 | 空気分離方法 |
US4543115A (en) * | 1984-02-21 | 1985-09-24 | Air Products And Chemicals, Inc. | Dual feed air pressure nitrogen generator cycle |
US5398514A (en) * | 1993-12-08 | 1995-03-21 | Praxair Technology, Inc. | Cryogenic rectification system with intermediate temperature turboexpansion |
US6000239A (en) * | 1998-07-10 | 1999-12-14 | Praxair Technology, Inc. | Cryogenic air separation system with high ratio turboexpansion |
US6053008A (en) * | 1998-12-30 | 2000-04-25 | Praxair Technology, Inc. | Method for carrying out subambient temperature, especially cryogenic, separation using refrigeration from a multicomponent refrigerant fluid |
US6112550A (en) * | 1998-12-30 | 2000-09-05 | Praxair Technology, Inc. | Cryogenic rectification system and hybrid refrigeration generation |
US8578734B2 (en) * | 2006-05-15 | 2013-11-12 | Shell Oil Company | Method and apparatus for liquefying a hydrocarbon stream |
JP5683277B2 (ja) | 2008-02-14 | 2015-03-11 | シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイShell Internationale Research Maatschappij Beslotenvennootshap | 炭化水素流の冷却方法及び装置 |
US20130000352A1 (en) * | 2011-06-30 | 2013-01-03 | General Electric Company | Air separation unit and systems incorporating the same |
CN109603186A (zh) * | 2018-12-14 | 2019-04-12 | 北京世纪隆博科技有限责任公司 | 一种精馏塔顶温与回流罐液位解耦控制方法 |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3066494A (en) * | 1958-05-26 | 1962-12-04 | Union Carbide Corp | Process of and apparatus for low-temperature separation of air |
US3264831A (en) * | 1962-01-12 | 1966-08-09 | Linde Ag | Method and apparatus for the separation of gas mixtures |
US3312074A (en) * | 1964-05-06 | 1967-04-04 | Hydrocarbon Research Inc | Air separation plant |
US3340697A (en) * | 1964-05-06 | 1967-09-12 | Hydrocarbon Research Inc | Heat exchange of crude oxygen and expanded high pressure nitrogen |
GB1314347A (en) * | 1970-03-16 | 1973-04-18 | Air Prod Ltd | Air rectification process for the production of oxygen |
BR7606681A (pt) * | 1975-10-28 | 1977-11-16 | Linde Ag | Processo e instalacao para fracionamento de ar |
JPS5449992A (en) * | 1977-09-28 | 1979-04-19 | Hitachi Ltd | Air separator |
JPS5545825A (en) * | 1978-09-21 | 1980-03-31 | Toray Industries | Dyeing of fiber structure |
-
1981
- 1981-12-09 US US06/328,817 patent/US4407135A/en not_active Expired - Lifetime
-
1982
- 1982-11-12 CA CA000415449A patent/CA1173737A/en not_active Expired
- 1982-12-06 KR KR8205465A patent/KR880001511B1/ko active
- 1982-12-07 BR BR8207103A patent/BR8207103A/pt not_active IP Right Cessation
- 1982-12-08 EP EP82850254A patent/EP0081473B2/en not_active Expired - Lifetime
- 1982-12-08 AT AT82850254T patent/ATE31809T1/de not_active IP Right Cessation
- 1982-12-08 DE DE8282850254T patent/DE3277931D1/de not_active Expired
- 1982-12-09 MX MX195534A patent/MX156853A/es unknown
- 1982-12-09 AU AU91705/82A patent/AU548184B2/en not_active Ceased
- 1982-12-09 ES ES518026A patent/ES518026A0/es active Granted
- 1982-12-09 JP JP57214733A patent/JPS58106377A/ja active Granted
- 1982-12-09 DK DK547282A patent/DK547282A/da not_active Application Discontinuation
- 1982-12-09 ZA ZA829072A patent/ZA829072B/xx unknown
- 1982-12-09 NO NO824149A patent/NO155828B/no unknown
Also Published As
Publication number | Publication date |
---|---|
EP0081473B1 (en) | 1988-01-07 |
AU548184B2 (en) | 1985-11-28 |
JPS627465B2 (ja) | 1987-02-17 |
JPS58106377A (ja) | 1983-06-24 |
EP0081473A2 (en) | 1983-06-15 |
AU9170582A (en) | 1983-06-16 |
DE3277931D1 (en) | 1988-02-11 |
DK547282A (da) | 1983-06-10 |
ZA829072B (en) | 1984-03-28 |
ES8402164A1 (es) | 1984-01-16 |
NO824149L (no) | 1983-06-10 |
KR840002973A (ko) | 1984-07-21 |
CA1173737A (en) | 1984-09-04 |
US4407135A (en) | 1983-10-04 |
EP0081473B2 (en) | 1993-07-14 |
KR880001511B1 (ko) | 1988-08-16 |
ES518026A0 (es) | 1984-01-16 |
ATE31809T1 (de) | 1988-01-15 |
MX156853A (es) | 1988-10-07 |
BR8207103A (pt) | 1983-10-11 |
EP0081473A3 (en) | 1984-12-27 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR0144129B1 (ko) | 기체 산소를 생성시키기 위한 저온 공기 분리 시스템 | |
US2873583A (en) | Dual pressure cycle for air separation | |
US4448595A (en) | Split column multiple condenser-reboiler air separation process | |
CA2186550C (en) | Process and apparatus for the production of moderate purity oxygen | |
KR100291684B1 (ko) | 공기의분리방법 | |
AU603157B2 (en) | Air separation | |
US5511381A (en) | Air separation | |
NO176221B (no) | Fremgangsmåte for ökning av argongjenvinning fra en blanding, f.eks. luft | |
KR880001510B1 (ko) | 산소막을 생산하는 공기분리 플랜트로부터 알곤을 회수하기 위한 방법 및 장치 | |
US5123249A (en) | Air separation | |
NO164739B (no) | Fremgangsmaate for fremstilling av store mengder nitrogen ved relativt hoeyt trykk. | |
KR100395848B1 (ko) | 고순도 산소 또는 저순도 산소를 생성하는 저온 정류 장치 | |
NO166224B (no) | Fremgangsmaate og innretning for fremstilling av gassformig nitrogen ved lavtemperaturdestillering av luft. | |
EP0742415B1 (en) | Process for removing nitrogen from LNG | |
KR20000011251A (ko) | 산소를제조하기위해공급공기의극저온정류를수행하는방법및장치 | |
NO155828B (no) | Fremgangsmaate for separering av luft ved rektifisering. | |
NO158116B (no) | Fremstilling av nitrogen ved kryogenseparering av luft. | |
US4783208A (en) | Air separation | |
US5263327A (en) | High recovery cryogenic rectification system | |
US2812645A (en) | Process and apparatus for separating gas mixtures | |
US4747859A (en) | Air separation | |
AU706680B2 (en) | Air separation | |
US3210947A (en) | Process for purifying gaseous streams by rectification | |
JPS61122479A (ja) | 窒素製造方法 | |
KR19990087937A (ko) | 일체식생성물보일러를갖춘극저온정류시스템 |