KR910018064A - 공기 분리 - Google Patents
공기 분리 Download PDFInfo
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- KR910018064A KR910018064A KR1019910006113A KR910006113A KR910018064A KR 910018064 A KR910018064 A KR 910018064A KR 1019910006113 A KR1019910006113 A KR 1019910006113A KR 910006113 A KR910006113 A KR 910006113A KR 910018064 A KR910018064 A KR 910018064A
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- heat exchange
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- low pressure
- liquid
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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
- 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
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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
- 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
- F25J3/042—Division of the main heat exchange line in consecutive sections having different functions having an intermediate feed connection
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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
- 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
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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
- 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
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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
- 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
- F25J3/04309—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 nitrogen
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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
- 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
- F25J3/04375—Details relating to the work expansion, e.g. process parameter etc.
- F25J3/04393—Details relating to the work expansion, e.g. process parameter etc. using multiple or multistage gas work expansion
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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
- 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
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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
- 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
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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
- 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
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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
- F25J2290/10—Mathematical formulae, modeling, plot or curves; Design methods
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- 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
- Y10S62/939—Partial feed stream expansion, air
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
내용 없음
Description
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제1도는 본 발명에 따른 첫번째, 방법 및 장치를 나타내는 공정 흐름도이다. 제2도는 본 발명에 따른 두번째 방법 및 장치를 나타내는 공정 흐름도이다. 제3도는 이중 정류관의 저압단에서 저압 강하 액체-증기 접촉 수단을 사용하여 종래의 공기 분리장치의 열교환기에 대한 온도에 대하여 도시된 열부하의 그래프이다.
Claims (11)
- 압축된 공기류의 온도를 열교환 수단에서 열교환에 의해 정류로 분리시키기에 적합한 값으로 감소시키고, 이로 인해 냉각된 공기류를 공기 분리용 이중 정류관의 고압단에 도입시키고(상기 이중 정류관은 저압단 및 고압단을 포함하고 있음), 상기 정류관의 고압단을 사용하여 액체 질소 환류 및 산소가 풍부한 공기 공급물을 저압단에 제공하고, 저압단으로부터 산소 생성물을 회수하는 것을 포함하고 있으며;이때 최소한 70%의 산소 생성물을 이중 정류관으로부터 기체로서 수득하고, 최소한 저압단이 균질 접촉으로 액체와 증기 사이에 물질 전달을 수행하기 위하여 이론적인 분리단 당 400Pa 이하의 압력강하를 갖는 액체-증기 접촉수단인 저압강하 액체-증기 접촉수단을 포함하고, 공기로부터 산소 생성물의 분리 방법을 위한 냉각이 외부일의 수행으로 유체의 최소한 2개의 분리 팽창을 수행함으로써 2단계로 일어나는데, 이때 이러한 제1팽창은 고온에서 열교환 수단으로부터 유체를 스득하고 저온에서 유체를 열교환 수단에 돌려 보내고(상기 온도는 둘다 열교환 수단의 냉각 말단부와 가온 말단부에서의 공기류의 온도 사이에 있음), 상기 제2팽창은 상기 압축된 공기류가 열교환 수단의 냉각 말단부를 나가는 온도 또는 그 이하의 가장 낮은 온도에서 유체를 생성시키는 공기로부터 산소 생성물을 분리하는 방법.
- 제1항에 있어서, 팽창중의 적어도 하나를 압축된 공기류로부터 얻은 압축된 공기로 수행하는 방법.
- 제1항 또는 제2항에 있어서, 제1팽창이 120내지 160K의 범위의 온도에서 유체를 생성시키는 방법.
- 제1항 내지 제3항중의 어느 한 항에 있어서, 제2팽창을 위한 유체를 120내지 160K범위의 온도에서 열교환수단으로부터 수득하는 방법.
- 제1항 내지 제4항중의 어느 한 항에 있어서, 팽창중의 하나를 정류관의 고압단으로부터 회수된 질소류로 수행하는 방법.
- 제1항 내지 제5항 중의 어느 한 항에 있어서, 산소 생성물을 전부 기체로서 수득하거나, 또는 10부피% 이하의 산소 생성물을 액체 상태로 수득하는 방법.
- 제1항 내지 제6항중의 어느 한 항에 있어서, 저압강하 액체-증기 접촉수단이 구조화된 팩킹(packing)을 포함하는 방법.
- 제1항 내지 제7항중의 어느 한 항에 있어서, 이중 정류관의 고압단이 4.5내지 5.5bar범위의 압력(단의 중간이상에서)에서 작동하는 방법.
- 주공기 압축기;주공기 압축기로부터 압축된 공기류를 정류에 의한 부리에 적합한 온도로 감소시키는 열교환 수단;저압단과 고압단을 갖는 이중 정류관(여기서, 고압단은 열교환 수단으로부터 압축된 공기류에 대한 출구 통하고 있으며, 최소한 저압단을 균질 접촉으로 액체와 증기사이에 물질전달을 수행하기 위해 이론적인 분리단 당 400Pa 이하의 압력강하를 갖는 액체 증기-접촉수단인 저압강하 액체-증기 접촉수단을 포함하고 있음);저압단 기부로부터 생성된 산소가 풍부한 유체 및 고압단 상부로 부터 생성된 액체 질소를 각각 저압단에 이동시키기 위한 저압단에서 고압단까지 연결된 도관;저압단으로부터 열교환 수단의 냉각 말단부로 산소 생성물 및 질소를 다시 돌려보냄으로써 산소 및 질소가 유입 공기에 대하여 향류 열교환 관계로 열교환 수단을 통해 다시 통과할수 있는 도관;사용시 고온에서 열교환 수단으로부터 유체를 수득하고 저온에서 그 유체를 상기 열교환수단으로 되돌려 보내는 장치에 냉각을 유발시키는 제1팽창 터어빈(여기서,상기 온도는 둘다 열교환 수단의 냉각 말단부와 가온 말단부에서의 공기류의 온도 사이에 있음);및 사용시 압축된 공기류가 열교환 수단의 냉각 말단부를 나가는 온도 또는 그 이하의 유출온도를 가짐으로써 최소한 70%의 산소 생성물을 기체로서 수득할 수있도록 산소 생성물 도관 또는 도관들이 배열된 제2팽창 터어빈을 포함하는 공기로부터산소 생성물을 분리하는 장치.
- 제9항에 있어서, 저압 액체-증기 접촉수단이 구조화된 팩킹을 포함하는 장치.
- ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB909008752A GB9008752D0 (en) | 1990-04-18 | 1990-04-18 | Air separation |
GB9008752.9 | 1990-04-18 |
Publications (2)
Publication Number | Publication Date |
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KR910018064A true KR910018064A (ko) | 1991-11-30 |
KR100190258B1 KR100190258B1 (ko) | 1999-06-01 |
Family
ID=10674633
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1019910006113A KR100190258B1 (ko) | 1990-04-18 | 1991-04-17 | 공기분리방법 |
Country Status (9)
Country | Link |
---|---|
US (1) | US5123249A (ko) |
EP (1) | EP0454327B2 (ko) |
JP (1) | JP3169627B2 (ko) |
KR (1) | KR100190258B1 (ko) |
CN (1) | CN1050418C (ko) |
CA (1) | CA2040796C (ko) |
DE (1) | DE69105601T3 (ko) |
GB (1) | GB9008752D0 (ko) |
ZA (1) | ZA912631B (ko) |
Families Citing this family (25)
Publication number | Priority date | Publication date | Assignee | Title |
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FR2688052B1 (fr) * | 1992-03-02 | 1994-05-20 | Maurice Grenier | Procede et installation de production d'oxygene et/ou d'azote gazeux sous pression par distillation d'air. |
FR2689223B1 (fr) * | 1992-03-24 | 1994-05-06 | Air Liquide | Procede et installation de transfert de fluide en provenance d'une colonne de distillation, notamment d'air. |
US5337570A (en) * | 1993-07-22 | 1994-08-16 | Praxair Technology, Inc. | Cryogenic rectification system for producing lower purity oxygen |
US5379598A (en) * | 1993-08-23 | 1995-01-10 | The Boc Group, Inc. | Cryogenic rectification process and apparatus for vaporizing a pumped liquid product |
FR2714721B1 (fr) * | 1993-12-31 | 1996-02-16 | Air Liquide | Procédé et installation de liquéfaction d'un gaz. |
FR2718518B1 (fr) * | 1994-04-12 | 1996-05-03 | Air Liquide | Procédé et installation pour la production de l'oxygène par distillation de l'air. |
US5758515A (en) * | 1997-05-08 | 1998-06-02 | Praxair Technology, Inc. | Cryogenic air separation with warm turbine recycle |
US5802873A (en) * | 1997-05-08 | 1998-09-08 | Praxair Technology, Inc. | Cryogenic rectification system with dual feed air turboexpansion |
US6006545A (en) * | 1998-08-14 | 1999-12-28 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes | Liquefier process |
FR2844344B1 (fr) * | 2002-09-11 | 2005-04-08 | Air Liquide | Installation de production de grandes quantites d'oxygene et/ou d'azote |
FR2865024B3 (fr) * | 2004-01-12 | 2006-05-05 | Air Liquide | Procede et installation de separation d'air par distillation cryogenique |
CN100357684C (zh) * | 2004-10-28 | 2007-12-26 | 苏州市兴鲁空分设备科技发展有限公司 | 一种空气分离的方法和装置 |
CN100357685C (zh) * | 2004-10-28 | 2007-12-26 | 苏州市兴鲁空分设备科技发展有限公司 | 一种空气分离的方法和装置 |
JP4515225B2 (ja) * | 2004-11-08 | 2010-07-28 | 大陽日酸株式会社 | 窒素製造方法及び装置 |
US8020408B2 (en) | 2006-12-06 | 2011-09-20 | Praxair Technology, Inc. | Separation method and apparatus |
FR2913760B1 (fr) * | 2007-03-13 | 2013-08-16 | Air Liquide | Procede et appareil de production de gaz de l'air sous forme gazeuse et liquide a haute flexibilite par distillation cryogenique |
DE102007031765A1 (de) * | 2007-07-07 | 2009-01-08 | Linde Ag | Verfahren zur Tieftemperaturzerlegung von Luft |
CN101464085B (zh) * | 2009-01-08 | 2011-01-26 | 北京名都厚德科技有限公司 | 一种超低压单塔深冷空分工艺 |
JP5647853B2 (ja) * | 2010-10-14 | 2015-01-07 | 大陽日酸株式会社 | 空気液化分離方法及び装置 |
TR201808162T4 (tr) * | 2014-07-05 | 2018-07-23 | Linde Ag | Havanın düşük sıcaklıkta ayrıştırılması vasıtasıyla bir basınçlı gaz ürününün kazanılmasına yönelik yöntem ve cihaz. |
EP3196574B1 (en) * | 2016-01-21 | 2021-05-05 | Linde GmbH | Process and apparatus for producing pressurized gaseous nitrogen by cryogenic separation of air |
JP6440232B1 (ja) * | 2018-03-20 | 2018-12-19 | レール・リキード−ソシエテ・アノニム・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード | 製品窒素ガスおよび製品アルゴンの製造方法およびその製造装置 |
EP3870915A1 (de) * | 2018-10-23 | 2021-09-01 | Linde GmbH | Verfahren und anlage zur tieftemperaturzerlegung von luft |
WO2021230912A1 (en) | 2020-05-11 | 2021-11-18 | Praxair Technology, Inc. | System and method for recovery of nitrogen, argon, and oxygen in moderate pressure cryogenic air separation unit |
EP4150276A1 (en) | 2020-05-15 | 2023-03-22 | Praxair Technology, Inc. | Integrated nitrogen liquefier for a nitrogen and argon producing cryogenic air separation unit |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3086371A (en) * | 1957-09-12 | 1963-04-23 | Air Prod & Chem | Fractionation of gaseous mixtures |
US4224045A (en) * | 1978-08-23 | 1980-09-23 | Union Carbide Corporation | Cryogenic system for producing low-purity oxygen |
DE2854508C2 (de) * | 1978-12-16 | 1981-12-03 | Linde Ag, 6200 Wiesbaden | Verfahren und Vorrichtung zur Tieftemperaturzerlegung eines Gasgemisches |
FR2461906A1 (fr) * | 1979-07-20 | 1981-02-06 | Air Liquide | Procede et installation cryogeniques de separation d'air avec production d'oxygene sous haute pression |
US4410343A (en) * | 1981-12-24 | 1983-10-18 | Union Carbide Corporation | Air boiling process to produce low purity oxygen |
US4555256A (en) * | 1982-05-03 | 1985-11-26 | Linde Aktiengesellschaft | Process and device for the production of gaseous oxygen at elevated pressure |
JPS61130769A (ja) * | 1984-11-30 | 1986-06-18 | 株式会社日立製作所 | 低温廃ガスを利用した寒冷発生方法 |
GB8622055D0 (en) * | 1986-09-12 | 1986-10-22 | Boc Group Plc | Air separation |
DE3738559A1 (de) * | 1987-11-13 | 1989-05-24 | Linde Ag | Verfahren zur luftzerlegung durch tieftemperaturrektifikation |
US4871382A (en) * | 1987-12-14 | 1989-10-03 | Air Products And Chemicals, Inc. | Air separation process using packed columns for oxygen and argon recovery |
US4836836A (en) * | 1987-12-14 | 1989-06-06 | Air Products And Chemicals, Inc. | Separating argon/oxygen mixtures using a structured packing |
ITMI20021467A1 (it) * | 2002-07-04 | 2004-01-05 | Francesco Paolo Terranova | Impianto per produrre energia elettrica dal movimento delle onde del mare |
-
1990
- 1990-04-18 GB GB909008752A patent/GB9008752D0/en active Pending
-
1991
- 1991-04-09 ZA ZA912631A patent/ZA912631B/xx unknown
- 1991-04-11 EP EP91303237A patent/EP0454327B2/en not_active Expired - Lifetime
- 1991-04-11 DE DE69105601T patent/DE69105601T3/de not_active Expired - Fee Related
- 1991-04-17 KR KR1019910006113A patent/KR100190258B1/ko not_active IP Right Cessation
- 1991-04-17 US US07/686,738 patent/US5123249A/en not_active Expired - Lifetime
- 1991-04-18 CN CN91102951A patent/CN1050418C/zh not_active Expired - Fee Related
- 1991-04-18 JP JP08681591A patent/JP3169627B2/ja not_active Expired - Fee Related
- 1991-04-18 CA CA002040796A patent/CA2040796C/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
CA2040796A1 (en) | 1991-10-19 |
JP3169627B2 (ja) | 2001-05-28 |
AU626752B2 (en) | 1992-08-06 |
CN1050418C (zh) | 2000-03-15 |
DE69105601D1 (de) | 1995-01-19 |
GB9008752D0 (en) | 1990-06-13 |
EP0454327B1 (en) | 1994-12-07 |
DE69105601T3 (de) | 2001-02-01 |
EP0454327B2 (en) | 2000-05-31 |
KR100190258B1 (ko) | 1999-06-01 |
US5123249A (en) | 1992-06-23 |
CA2040796C (en) | 2001-12-25 |
AU7435791A (en) | 1991-10-24 |
EP0454327A1 (en) | 1991-10-30 |
DE69105601T2 (de) | 1995-04-27 |
ZA912631B (en) | 1992-01-29 |
JPH0626759A (ja) | 1994-02-04 |
CN1056566A (zh) | 1991-11-27 |
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