DE69910272D1 - Kryogenisches Rektifikationsystem zur Herstellung von ultrahochreinem Stickstoff und ultrahochreinem Sauerstoff - Google Patents
Kryogenisches Rektifikationsystem zur Herstellung von ultrahochreinem Stickstoff und ultrahochreinem SauerstoffInfo
- Publication number
- DE69910272D1 DE69910272D1 DE69910272T DE69910272T DE69910272D1 DE 69910272 D1 DE69910272 D1 DE 69910272D1 DE 69910272 T DE69910272 T DE 69910272T DE 69910272 T DE69910272 T DE 69910272T DE 69910272 D1 DE69910272 D1 DE 69910272D1
- Authority
- DE
- Germany
- Prior art keywords
- high purity
- ultra high
- production
- rectification system
- cryogenic rectification
- 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 - Fee Related
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
- F25J3/04284—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
-
- 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
- F25J3/04436—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 at least a triple pressure main column system
- F25J3/04454—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 at least a triple pressure main column system a main column system not otherwise provided, e.g. serially coupling of columns or more than three pressure levels
-
- 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
- F25J2200/20—Processes or apparatus using separation by rectification in an elevated pressure multiple column system wherein the lowest pressure column is at a pressure well above the minimum pressure needed to overcome pressure drop to reject the products to atmosphere
-
- 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
- F25J2200/32—Processes or apparatus using separation by rectification using a side column fed by a stream from the 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
- F25J2200/34—Processes or apparatus using separation by rectification using a side column fed by a stream from the 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
- F25J2215/00—Processes characterised by the type or other details of the product stream
- F25J2215/42—Nitrogen or special cases, e.g. multiple or low purity N2
- F25J2215/44—Ultra high purity nitrogen, i.e. generally less than 1 ppb impurities
-
- 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
- F25J2215/00—Processes characterised by the type or other details of the product stream
- F25J2215/50—Oxygen or special cases, e.g. isotope-mixtures or low purity O2
- F25J2215/56—Ultra high purity oxygen, i.e. generally more than 99,9% O2
-
- 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
- F25J2235/00—Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams
- F25J2235/42—Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams the 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
- F25J2245/00—Processes or apparatus involving steps for recycling of process streams
- F25J2245/42—Processes or apparatus involving steps for recycling of process streams the recycled stream being nitrogen
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)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/024,196 US5918482A (en) | 1998-02-17 | 1998-02-17 | Cryogenic rectification system for producing ultra-high purity nitrogen and ultra-high purity oxygen |
US24196 | 1998-02-17 |
Publications (2)
Publication Number | Publication Date |
---|---|
DE69910272D1 true DE69910272D1 (de) | 2003-09-18 |
DE69910272T2 DE69910272T2 (de) | 2004-06-17 |
Family
ID=21819354
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE69910272T Expired - Fee Related DE69910272T2 (de) | 1998-02-17 | 1999-02-16 | Kryogenisches Rektifikationsystem zur Herstellung von ultrahochreinem Stickstoff und ultrahochreinem Sauerstoff |
Country Status (10)
Country | Link |
---|---|
US (1) | US5918482A (de) |
EP (1) | EP0936429B1 (de) |
JP (1) | JP3545629B2 (de) |
KR (1) | KR100407184B1 (de) |
CN (1) | CN1123753C (de) |
BR (1) | BR9900646A (de) |
CA (1) | CA2262238A1 (de) |
DE (1) | DE69910272T2 (de) |
ES (1) | ES2200417T3 (de) |
ID (1) | ID23302A (de) |
Families Citing this family (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5934104A (en) * | 1998-06-02 | 1999-08-10 | Air Products And Chemicals, Inc. | Multiple column nitrogen generators with oxygen coproduction |
US6173586B1 (en) | 1999-08-31 | 2001-01-16 | Praxair Technology, Inc. | Cryogenic rectification system for producing very high purity oxygen |
US6327873B1 (en) | 2000-06-14 | 2001-12-11 | Praxair Technology Inc. | Cryogenic rectification system for producing ultra high purity oxygen |
US6397631B1 (en) | 2001-06-12 | 2002-06-04 | Air Products And Chemicals, Inc. | Air separation process |
US6460373B1 (en) | 2001-12-04 | 2002-10-08 | Praxair Technology, Inc. | Cryogenic rectification system for producing high purity oxygen |
US7284395B2 (en) * | 2004-09-02 | 2007-10-23 | Praxair Technology, Inc. | Cryogenic air separation plant with reduced liquid drain loss |
US20080127676A1 (en) * | 2006-11-30 | 2008-06-05 | Amcscorporation | Method and apparatus for production of high-pressure nitrogen from air by cryogenic distillation |
US9103587B2 (en) * | 2009-12-17 | 2015-08-11 | L'Air Liquide Société Anonyme pour l'Etude et l'Exploitation des Procedes Georges Claude | Process and apparatus for the separation of air by cryogenic distillation |
JP5205436B2 (ja) * | 2010-10-29 | 2013-06-05 | 株式会社シマノ | 自転車用モータ制御システム |
US9097459B2 (en) * | 2011-08-17 | 2015-08-04 | Air Liquide Process & Construction, Inc. | Production of high-pressure gaseous nitrogen |
CN102506559A (zh) * | 2011-09-28 | 2012-06-20 | 开封东京空分集团有限公司 | 多段精馏制取高纯氮气空分工艺 |
CN104048478B (zh) * | 2014-06-23 | 2016-03-30 | 浙江大川空分设备有限公司 | 高提取率和低能耗污氮气提纯氮气的设备及其提取方法 |
CN113566495B (zh) * | 2021-07-28 | 2022-04-26 | 杭州特盈能源技术发展有限公司 | 一种玻璃窑炉用低能耗氮氧制取工艺 |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2535489C3 (de) * | 1975-08-08 | 1978-05-24 | Linde Ag, 6200 Wiesbaden | Verfahren und Vorrichtung zur Zerlegung eines tiefsiedenden Gasgemisches |
US4560397A (en) * | 1984-08-16 | 1985-12-24 | Union Carbide Corporation | Process to produce ultrahigh purity oxygen |
US4755202A (en) * | 1987-07-28 | 1988-07-05 | Union Carbide Corporation | Process and apparatus to produce ultra high purity oxygen from a gaseous feed |
US4780118A (en) * | 1987-07-28 | 1988-10-25 | Union Carbide Corporation | Process and apparatus to produce ultra high purity oxygen from a liquid feed |
US4902321A (en) * | 1989-03-16 | 1990-02-20 | Union Carbide Corporation | Cryogenic rectification process for producing ultra high purity nitrogen |
US5049173A (en) * | 1990-03-06 | 1991-09-17 | Air Products And Chemicals, Inc. | Production of ultra-high purity oxygen from cryogenic air separation plants |
US5098457A (en) * | 1991-01-22 | 1992-03-24 | Union Carbide Industrial Gases Technology Corporation | Method and apparatus for producing elevated pressure nitrogen |
US5195324A (en) * | 1992-03-19 | 1993-03-23 | Prazair Technology, Inc. | Cryogenic rectification system for producing nitrogen and ultra high purity oxygen |
JP2966999B2 (ja) * | 1992-04-13 | 1999-10-25 | 日本エア・リキード株式会社 | 超高純度窒素・酸素製造装置 |
US5528906A (en) * | 1995-06-26 | 1996-06-25 | The Boc Group, Inc. | Method and apparatus for producing ultra-high purity oxygen |
US5582032A (en) * | 1995-08-11 | 1996-12-10 | Liquid Air Engineering Corporation | Ultra-high purity oxygen production |
US5590543A (en) * | 1995-08-29 | 1997-01-07 | Air Products And Chemicals, Inc. | Production of ultra-high purity oxygen from cryogenic air separation plants |
-
1998
- 1998-02-17 US US09/024,196 patent/US5918482A/en not_active Expired - Lifetime
-
1999
- 1999-02-04 ID IDP990080D patent/ID23302A/id unknown
- 1999-02-12 KR KR10-1999-0004996A patent/KR100407184B1/ko not_active IP Right Cessation
- 1999-02-12 BR BR9900646-4A patent/BR9900646A/pt not_active Application Discontinuation
- 1999-02-14 CN CN99102216A patent/CN1123753C/zh not_active Expired - Fee Related
- 1999-02-16 ES ES99103064T patent/ES2200417T3/es not_active Expired - Lifetime
- 1999-02-16 JP JP03717799A patent/JP3545629B2/ja not_active Expired - Fee Related
- 1999-02-16 CA CA002262238A patent/CA2262238A1/en not_active Abandoned
- 1999-02-16 EP EP99103064A patent/EP0936429B1/de not_active Expired - Lifetime
- 1999-02-16 DE DE69910272T patent/DE69910272T2/de not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
CN1123753C (zh) | 2003-10-08 |
ID23302A (id) | 2000-04-05 |
CN1226673A (zh) | 1999-08-25 |
DE69910272T2 (de) | 2004-06-17 |
EP0936429A3 (de) | 1999-11-24 |
KR19990072641A (ko) | 1999-09-27 |
JPH11316080A (ja) | 1999-11-16 |
CA2262238A1 (en) | 1999-08-17 |
EP0936429B1 (de) | 2003-08-13 |
BR9900646A (pt) | 1999-12-28 |
ES2200417T3 (es) | 2004-03-01 |
EP0936429A2 (de) | 1999-08-18 |
US5918482A (en) | 1999-07-06 |
JP3545629B2 (ja) | 2004-07-21 |
KR100407184B1 (ko) | 2003-11-28 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE69218542T3 (de) | Kryogenisches Destillationsverfahren zur Herstellung von Sauerstoff und Stickstoff | |
DE69502328T2 (de) | Kryogenisches Rektifikationsverfahren zur Herstellung von Hochdruckstickstoff | |
DE69206956D1 (de) | Kryogenisches Rektifikationssystem zur Herstellung von ultrahochreinem Sauerstoff | |
DE69713002T2 (de) | Kryogenisches System zur Herstellung von Stickstoff | |
DE69511028D1 (de) | Kryogenes Rektifikationssystem mit Seitenkolonne zur Herstellung von niedrigreinem Sauerstoff | |
DE69910272D1 (de) | Kryogenisches Rektifikationsystem zur Herstellung von ultrahochreinem Stickstoff und ultrahochreinem Sauerstoff | |
DE69415656D1 (de) | Verfahren zur herstellung von hochreinem und ultrareinem bisphenol-a | |
BR9402897A (pt) | Processo e aparelho de retificação criogênica para produzir oxigênio de pureza inferior. | |
DE69608057T2 (de) | Kryogenisches Rektifikationssystem zur Herstellung von Sauerstoff mit zweierlei Reinheit | |
SG49367A1 (en) | Three column cryogenic cycle for the production of impure oxygen and pure nitrogen | |
DE69717402D1 (de) | Kryogenisches Rektifikationssystem zur Herstellung von Sauerstoff niedrigerer und höherer Reinheit | |
DE69301046D1 (de) | Kryogenisches Rektifikationsverfahren zur Herstellung von Stickstoff und reinstem Sauerstoff | |
BR9703752A (pt) | Sistema de retificação criogénica para a produção de oxigénio com baixa pureza e nitrogénio de alta pureza | |
DE69704980D1 (de) | Ultrahochreiner Stickstoff- und Sauerstoffgenerator | |
DE69613066D1 (de) | Kryogenische Lufttrennungsanlage zur Herstellung von ultrahochreinem Sauerstoff | |
DE69505731T2 (de) | Kryogenes Rektifikationsverfahren von Luft zur Herstellung von Hochdrucksauerstoff | |
BR9701156A (pt) | Sistema de retificação criogênica para a produção de oxigênio gasoso de menor pureza e oxigênio de alta pureza | |
DE69107165T2 (de) | Kryogenes lufttrenunnungsverfahren zur herstellung von sauerstoff und mitteldruckstickstoff. | |
DE69619455T2 (de) | Herstellung von ultrahochreinem Sauerstoff | |
DE69710824T2 (de) | Kryogenisches Rektifikationssystem mit Seitenkolonne zur Herstellung von Sauerstoff niedrigerer Reinheit und hochreinem Stickstoff | |
DE69713042D1 (de) | Kryogenisches Rektifikationssystem zur Herstellung von Argon und Sauerstoff niedriger Reinheit | |
SG49369A1 (en) | Ultra high purity oxygen distillation unit integrated with ultra high purity nitrogen purifier | |
DE60005253D1 (de) | Kryogenisches Rektifikationssystem zur Herstellung von Sauerstoff mit variabler Produktionsrate | |
DE69618100D1 (de) | Gasgenerator zur Herstellung von hochreinem Stickstoff | |
GB9800017D0 (en) | Production of high purity nitrogen or oxygen from air |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
8364 | No opposition during term of opposition | ||
8339 | Ceased/non-payment of the annual fee |