ES2096124T3 - Sistema de rectificacion criogenica con recuperacion elevada. - Google Patents
Sistema de rectificacion criogenica con recuperacion elevada.Info
- Publication number
- ES2096124T3 ES2096124T3 ES93104981T ES93104981T ES2096124T3 ES 2096124 T3 ES2096124 T3 ES 2096124T3 ES 93104981 T ES93104981 T ES 93104981T ES 93104981 T ES93104981 T ES 93104981T ES 2096124 T3 ES2096124 T3 ES 2096124T3
- Authority
- ES
- Spain
- Prior art keywords
- rectification system
- cryogenic rectification
- high recovery
- pressure column
- recovery
- 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 - Lifetime
Links
- 238000011084 recovery Methods 0.000 title abstract 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract 1
- 239000012530 fluid Substances 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 229910052757 nitrogen Inorganic materials 0.000 abstract 1
- 239000001301 oxygen Substances 0.000 abstract 1
- 229910052760 oxygen Inorganic materials 0.000 abstract 1
- 238000010992 reflux Methods 0.000 abstract 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
- 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
- F25J3/04248—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
- F25J3/04248—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
-
- 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
- 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
- F25J2250/52—One fluid being oxygen enriched compared to air, e.g. "crude 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
- Y10S62/939—Partial feed stream expansion, 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)
Abstract
UN SISTEMA DE RECTIFICACION CRIOGENICO EN DONDE LIQUIDO (107) ENRIQUECIDO CON OXIGENO PROCEDENTE DE UNA COLUMNA A PRESION MAS ELEVADA (212) ES VAPORIZADO EN PRESENCIA DE FLUIDO (208) QUE CONTIENE NITROGENO CONDENSADO, EL CUAL ES EMPLEADO COMO REFLUJO ADICIONAL (160) EN LA COLUMNA DE PRESION INFERIOR (210), AUMENTANDO DE ESE MODO LA RELACION L/V Y LA RECUPERACION DEL PRODUCTO.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/858,212 US5263327A (en) | 1992-03-26 | 1992-03-26 | High recovery cryogenic rectification system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| ES2096124T3 true ES2096124T3 (es) | 1997-03-01 |
| ES2096124T5 ES2096124T5 (es) | 2000-06-16 |
Family
ID=25327763
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES93104981T Expired - Lifetime ES2096124T5 (es) | 1992-03-26 | 1993-03-25 | Sistema de rectificacion criogenica con recuperacion elevada. |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US5263327A (es) |
| EP (1) | EP0563800B2 (es) |
| BR (1) | BR9301311A (es) |
| CA (1) | CA2092454C (es) |
| DE (1) | DE69306995T3 (es) |
| ES (1) | ES2096124T5 (es) |
| NO (1) | NO180696C (es) |
| ZA (1) | ZA932139B (es) |
Families Citing this family (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0636845B1 (en) * | 1993-04-30 | 1999-07-28 | The BOC Group plc | Air separation |
| GB9405071D0 (en) * | 1993-07-05 | 1994-04-27 | Boc Group Plc | Air separation |
| GB9326168D0 (en) * | 1993-12-22 | 1994-02-23 | Bicc Group The Plc | Air separation |
| US5386691A (en) * | 1994-01-12 | 1995-02-07 | Praxair Technology, Inc. | Cryogenic air separation system with kettle vapor bypass |
| US5386692A (en) * | 1994-02-08 | 1995-02-07 | Praxair Technology, Inc. | Cryogenic rectification system with hybrid product boiler |
| US5551258A (en) * | 1994-12-15 | 1996-09-03 | The Boc Group Plc | Air separation |
| GB9521782D0 (en) * | 1995-10-24 | 1996-01-03 | Boc Group Plc | Air separation |
| US5600970A (en) * | 1995-12-19 | 1997-02-11 | Praxair Technology, Inc. | Cryogenic rectification system with nitrogen turboexpander heat pump |
| US5675977A (en) * | 1996-11-07 | 1997-10-14 | Praxair Technology, Inc. | Cryogenic rectification system with kettle liquid column |
| US5956973A (en) * | 1997-02-11 | 1999-09-28 | Air Products And Chemicals, Inc. | Air separation with intermediate pressure vaporization and expansion |
| US6009723A (en) * | 1998-01-22 | 2000-01-04 | Air Products And Chemicals, Inc. | Elevated pressure air separation process with use of waste expansion for compression of a process stream |
| US6286336B1 (en) | 2000-05-03 | 2001-09-11 | Praxair Technology, Inc. | Cryogenic air separation system for elevated pressure product |
| US7135341B2 (en) * | 2004-04-07 | 2006-11-14 | Beckman Coulter, Inc. | Reference control containing a nucleated red blood cell component |
| US9970389B2 (en) * | 2014-03-06 | 2018-05-15 | The Boeing Company | Antivortex device and method of assembling thereof |
Family Cites Families (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3348385A (en) * | 1964-12-23 | 1967-10-24 | Gas Equipment Engineering Corp | Separation of gas mixtures |
| GB1182615A (en) * | 1967-06-01 | 1970-02-25 | Roman Stoklosinski | Improvements in or relating to the Separation of Mixtures of Gases |
| US4137056A (en) * | 1974-04-26 | 1979-01-30 | Golovko Georgy A | Process for low-temperature separation of air |
| US4224045A (en) * | 1978-08-23 | 1980-09-23 | Union Carbide Corporation | Cryogenic system for producing low-purity oxygen |
| US4357153A (en) * | 1981-03-30 | 1982-11-02 | Erickson Donald C | Internally heat pumped single pressure distillative separations |
| GB2129115B (en) * | 1982-10-27 | 1986-03-12 | Air Prod & Chem | Producing gaseous nitrogen |
| US4560397A (en) * | 1984-08-16 | 1985-12-24 | Union Carbide Corporation | Process to produce ultrahigh purity oxygen |
| US4615716A (en) * | 1985-08-27 | 1986-10-07 | Air Products And Chemicals, Inc. | Process for producing ultra high purity oxygen |
| GB8524598D0 (en) * | 1985-10-04 | 1985-11-06 | Boc Group Plc | Liquid-vapour contact |
| US4655809A (en) * | 1986-01-10 | 1987-04-07 | Air Products And Chemicals, Inc. | Air separation process with single distillation column with segregated heat pump cycle |
| US4705548A (en) * | 1986-04-25 | 1987-11-10 | Air Products And Chemicals, Inc. | Liquid products using an air and a nitrogen recycle liquefier |
| US4662918A (en) * | 1986-05-30 | 1987-05-05 | Air Products And Chemicals, Inc. | Air separation process |
| DE3871220D1 (de) * | 1987-04-07 | 1992-06-25 | Boc Group Plc | Lufttrennung. |
| GB8904275D0 (en) * | 1989-02-24 | 1989-04-12 | Boc Group Plc | Air separation |
| US4947649A (en) * | 1989-04-13 | 1990-08-14 | Air Products And Chemicals, Inc. | Cryogenic process for producing low-purity oxygen |
| US4936099A (en) * | 1989-05-19 | 1990-06-26 | Air Products And Chemicals, Inc. | Air separation process for the production of oxygen-rich and nitrogen-rich products |
-
1992
- 1992-03-26 US US07/858,212 patent/US5263327A/en not_active Expired - Lifetime
-
1993
- 1993-03-25 CA CA002092454A patent/CA2092454C/en not_active Expired - Fee Related
- 1993-03-25 BR BR9301311A patent/BR9301311A/pt not_active IP Right Cessation
- 1993-03-25 EP EP93104981A patent/EP0563800B2/en not_active Expired - Lifetime
- 1993-03-25 ZA ZA932139A patent/ZA932139B/xx unknown
- 1993-03-25 DE DE69306995T patent/DE69306995T3/de not_active Expired - Fee Related
- 1993-03-25 ES ES93104981T patent/ES2096124T5/es not_active Expired - Lifetime
- 1993-03-25 NO NO931115A patent/NO180696C/no unknown
Also Published As
| Publication number | Publication date |
|---|---|
| DE69306995D1 (de) | 1997-02-13 |
| NO180696C (no) | 1997-05-28 |
| EP0563800B2 (en) | 2000-04-12 |
| BR9301311A (pt) | 1993-09-28 |
| ZA932139B (en) | 1993-10-14 |
| DE69306995T3 (de) | 2000-08-17 |
| NO931115D0 (no) | 1993-03-25 |
| NO931115L (no) | 1993-09-27 |
| ES2096124T5 (es) | 2000-06-16 |
| EP0563800A1 (en) | 1993-10-06 |
| CA2092454C (en) | 1996-05-28 |
| NO180696B (no) | 1997-02-17 |
| US5263327A (en) | 1993-11-23 |
| DE69306995T2 (de) | 1997-06-26 |
| CA2092454A1 (en) | 1993-09-27 |
| EP0563800B1 (en) | 1997-01-02 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| ES2096124T3 (es) | Sistema de rectificacion criogenica con recuperacion elevada. | |
| ES2057671T3 (es) | Separacion criogenica del aire con hervidor doble de producto. | |
| ES2072054T5 (es) | Metodo de rectificacion criogenica para producir argon refinado. | |
| ES2072099T3 (es) | Proceso y sistema de separacion criogenica de aire. | |
| ES2037416T3 (es) | Un procedimiento para incrementar la recuperacion de argon a partir de la separacion de una mezcla que comprende oxigeno, nitrogeno y argon. | |
| ES2104025T3 (es) | Sistema de produccion criogenica de helio. | |
| MX9302266A (es) | Sistema de rectificacion criogenica de triple columna. | |
| ES2187702T3 (es) | Sistema de rectificacion criogenica con columna de liquido de caldera. | |
| MX9205750A (es) | Proceso y sistema de adsorcion con presion variable, de doble producto. | |
| ES2130355T3 (es) | Separacion de aire. | |
| ES2071879T5 (es) | Metodo y sistema mejorados de enriquecimiento en oxigeno. | |
| ES2134391T3 (es) | Sistema de rectificacion criogenica de columna lateral para producir oxigeno de menor pureza. | |
| ES2085725T3 (es) | Procedimiento de destilacion para la produccion de nitrogeno libre de monoxido de carbono. | |
| ES2037318T3 (es) | Metodo de control para aumento de la recuperacion del argon desde unidades de separacion de aire criogenico. | |
| ES2145967T3 (es) | Proceso e instalacion de separacion de aire. | |
| ES2093946T3 (es) | Procedimiento e instalacion de produccion de al menos un producto gaseoso bajo presion y al menos un liquido por destilacion de aire. | |
| DE69320116D1 (de) | Lufttrennung | |
| ES2123719T5 (es) | Procedimiento y aparato de separacion criogenica de aire que produce nitrogeno a alta presion mediante nitrogeno liquido bombeado. | |
| ES2030311T5 (es) | Procedimiento e instalacion de separacion de aire y de produccion de oxigeno ultrapuro. | |
| ES2123179T3 (es) | Sistema de rectificacion criogenica con ebullicion de aire para la produccion de oxigeno a presion elevada. | |
| ES2043442T3 (es) | Procedimiento y dispositivo de separacion dinamica de dos zonas. | |
| MX9300286A (es) | Sistema de rectificacion criogenica para producir un producto de presion elevada. | |
| DE69200178D1 (de) | Kryogenverfahren zur Zerlegung von Sauerstoff enthaltenden Mischungen, strukturierte Packung zur Verwendung im selben und Luftdestillationskolonne mit derartiger Packung. | |
| ES2067930T3 (es) | Metodo de separacion criogenica de aire para la produccion de oxigeno y nitrogeno a presion media. | |
| ES2077085T3 (es) | Produccion de argon a partir de aire con escaso contenido en oxigeno. |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FG2A | Definitive protection |
Ref document number: 563800 Country of ref document: ES |