ES2171509T3 - Procedimiento e instalacion de separacion de una mezcla gaseosa por destilacion criogena. - Google Patents

Procedimiento e instalacion de separacion de una mezcla gaseosa por destilacion criogena.

Info

Publication number
ES2171509T3
ES2171509T3 ES95400804T ES95400804T ES2171509T3 ES 2171509 T3 ES2171509 T3 ES 2171509T3 ES 95400804 T ES95400804 T ES 95400804T ES 95400804 T ES95400804 T ES 95400804T ES 2171509 T3 ES2171509 T3 ES 2171509T3
Authority
ES
Spain
Prior art keywords
distillation
criogena
separation
procedure
installation
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
Application number
ES95400804T
Other languages
English (en)
Inventor
Norbert Rieth
Bernard Darredeau
Jean-Yves Lehman
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
Original Assignee
LAir Liquide SA a Directoire et Conseil de Surveillance pour lEtude et lExploitation des Procedes Georges Claude
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=26231111&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=ES2171509(T3) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by LAir Liquide SA a Directoire et Conseil de Surveillance pour lEtude et lExploitation des Procedes Georges Claude filed Critical LAir Liquide SA a Directoire et Conseil de Surveillance pour lEtude et lExploitation des Procedes Georges Claude
Application granted granted Critical
Publication of ES2171509T3 publication Critical patent/ES2171509T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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
    • F25J3/04763—Start-up or control of the process; Details of the apparatus used
    • F25J3/04769—Operation, control and regulation of the process; Instrumentation within the process
    • F25J3/04787—Heat exchange, e.g. main heat exchange line; Subcooler, external reboiler-condenser
    • 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
    • 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
    • F25J3/04006—Providing pressurised feed air or process streams within or from the air fractionation unit
    • F25J3/04012—Providing pressurised feed air or process streams within or from the air fractionation unit by compression of warm gaseous streams; details of intake or interstage cooling
    • F25J3/04018—Providing pressurised feed air or process streams within or from the air fractionation unit by compression of warm gaseous streams; details of intake or interstage cooling of main feed 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
    • F25J3/04006—Providing pressurised feed air or process streams within or from the air fractionation unit
    • F25J3/04109—Arrangements of compressors and /or their drivers
    • F25J3/04139—Combination of different types of drivers mechanically coupled to the same compressor, possibly split on multiple compressor casings
    • 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
    • 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
    • F25J3/04406—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
    • F25J3/04763—Start-up or control of the process; Details of the apparatus used
    • F25J3/04769—Operation, control and regulation of the process; Instrumentation within the process
    • F25J3/04812—Different modes, i.e. "runs" of operation
    • F25J3/04836—Variable air feed, i.e. "load" or product demand during specified periods, e.g. during periods with high respectively low power costs
    • 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
    • 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
    • F25J2290/32—Details on header or distribution passages of heat exchangers, e.g. of reboiler-condenser or plate heat exchangers

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

CON EL FIN DE AUMENTAR LA PRODUCCION DE UN APARATO DE DESTILACION (15), QUE CONTIENE REVESTIMIENTOS ESTRUTURADOS, DE UN VALOR POR ENCIMA DE LA PRODUCCION NOMINAL SE PREVEN MEDIOS (1,3) PARA AUMENTAR LA PRESION DE FUNCIONAMIENTO DEL APARATO DE MANERA A AUMENTAR EL LIMITE DE OBSTRUCCION DEL APARATO EN PROPORCIONES CERCANAS. LA DISTRIBUCION DE LOS PASOS DEL INTERCAMBIADOR PRINCIPAL (9) PUEDE VARIAR SEGUN EL REGIMEN DE PRODUCCION ESTABLECIDO.
ES95400804T 1994-04-22 1995-04-10 Procedimiento e instalacion de separacion de una mezcla gaseosa por destilacion criogena. Expired - Lifetime ES2171509T3 (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR9404865A FR2718977B1 (fr) 1994-04-22 1994-04-22 Procédé et installation de séparation d'un mélange gazeux par distillation cryogénique.
US08/393,265 US5548975A (en) 1994-04-22 1995-02-23 Process and installation for the separation of a gaseous mixture by cryogenic distillation

Publications (1)

Publication Number Publication Date
ES2171509T3 true ES2171509T3 (es) 2002-09-16

Family

ID=26231111

Family Applications (1)

Application Number Title Priority Date Filing Date
ES95400804T Expired - Lifetime ES2171509T3 (es) 1994-04-22 1995-04-10 Procedimiento e instalacion de separacion de una mezcla gaseosa por destilacion criogena.

Country Status (14)

Country Link
US (1) US5548975A (es)
EP (1) EP0678317B1 (es)
JP (1) JP3784854B2 (es)
CN (1) CN1097716C (es)
AU (1) AU685230B2 (es)
BR (1) BR9501745A (es)
CA (1) CA2147573C (es)
CZ (1) CZ103195A3 (es)
DE (1) DE69525482T2 (es)
ES (1) ES2171509T3 (es)
FI (1) FI951832A (es)
FR (1) FR2718977B1 (es)
PL (1) PL308286A1 (es)
ZA (1) ZA952947B (es)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1045543C (zh) * 1995-10-24 1999-10-13 永济电机厂 废丙酮、甲苯溶剂综合提纯装置
US5921109A (en) * 1998-10-21 1999-07-13 Praxair Technology, Inc. Method for operating a cryogenic rectification column
US6212907B1 (en) 2000-02-23 2001-04-10 Praxair Technology, Inc. Method for operating a cryogenic rectification column
FR2880418B1 (fr) * 2004-12-30 2007-04-27 Air Liquide Ensemble d'echangeurs de chaleur, appareil de distillation cryogenique incorporant un tel ensemble et procede de distillation cryogenique utilisant un tel ensemble
CN106440659A (zh) * 2016-08-19 2017-02-22 浙江智海化工设备工程有限公司 一种低能耗内压缩空分装置
FR3075658B1 (fr) * 2017-12-21 2022-01-28 Air Liquide Procede de limitation de la concentration d'oxygene contenu dans un courant de biomethane
CN110478930B (zh) * 2019-08-21 2021-05-04 乐平市瑞盛制药有限公司 一种分馏塔

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5076823A (en) * 1990-03-20 1991-12-31 Air Products And Chemicals, Inc. Process for cryogenic air separation
DE4030749A1 (de) * 1990-09-28 1992-04-02 Linde Ag Verfahren zur tieftemperaturzerlegung von luft
US5282365A (en) * 1992-11-17 1994-02-01 Praxair Technology, Inc. Packed column distillation system

Also Published As

Publication number Publication date
JPH0861842A (ja) 1996-03-08
CA2147573C (fr) 2006-12-05
CZ103195A3 (en) 1995-12-13
EP0678317A1 (fr) 1995-10-25
FI951832A (fi) 1995-10-23
FR2718977B1 (fr) 1996-06-07
PL308286A1 (en) 1995-10-30
CN1097716C (zh) 2003-01-01
DE69525482T2 (de) 2002-10-10
US5548975A (en) 1996-08-27
BR9501745A (pt) 1995-11-14
JP3784854B2 (ja) 2006-06-14
CN1112670A (zh) 1995-11-29
DE69525482D1 (de) 2002-03-28
CA2147573A1 (fr) 1995-10-23
EP0678317B1 (fr) 2002-02-20
ZA952947B (en) 1995-12-20
AU1639395A (en) 1995-11-02
FI951832A0 (fi) 1995-04-18
FR2718977A1 (fr) 1995-10-27
AU685230B2 (en) 1998-01-15

Similar Documents

Publication Publication Date Title
AR012080A1 (es) Metodo para producir pasajes dentro de un componente de turbomaquinarias y un componente de turbomaquinaria
BG104273A (en) Encoding of information consisting of multiple words by separation by words
ES2171509T3 (es) Procedimiento e instalacion de separacion de una mezcla gaseosa por destilacion criogena.
AR019562A1 (es) Sintesis de metanol
ES2131120T3 (es) Proceso para la preparacion de 3-(metiltio)propanal.
ATE24345T1 (de) Rohrverbindung.
BR9903378A (pt) Processo para a operação de uma coluna de retificação criogênica.
AR007156A1 (es) Procedimiento para inhibir o retardar la formacion o aglomeracion de hidratos en un efluente de produccion
CA2255167A1 (fr) Procede de liquefaction d'un gaz, notamment un gaz naturel ou air, comportant une purge a moyenne pression et son application
CO4950531A1 (es) Analogos de la vitamina d3 composciiones farmaceuticas que los contienen
ES2127532T3 (es) Preparacion de nalbufina con niveles bajos del epimero beta.
AU1326000A (en) A method for preventing or retarding the formation of gas hydrates
ES2093880T3 (es) Procedimiento y aparato para la recuperacion separada de un gas de alto peso molecular y un gas de bajo peso molecular a partir de una mezcla gaseosa inicial.
EP0714938A3 (en) Polyketone stabilization
ES2173103T3 (es) Un policarbonato ramificado y un proceso para su preparacion.
ES2140459T3 (es) Lubricantes mezclados de ester-polioles para fluidos refrigerantes de transmision de calor.
ES2026731T5 (es) Dispositivo de conexion con el aire exterior y de seguridad contra el llenado excesivo, para depositos.
GB190920882A (en) Improvements in Electric Hand Lamps.
EA199800001A1 (ru) Составные основные и вспомогательные уплотнения с контактирующими выпуклыми поверхностями
ES540730A0 (es) Procedimiento e instalacion para la obtencion de soluciones de tipo hidrocarburo clorofluorado con alto contenido de gas disuelto.
JPS57126833A (en) Crosslinkable polyolefin composition
JPS5224158A (en) Gas producer
ES274452U (es) Una disposicion de union de tubo y adaptador, en particular para instalaciones sanitarias y de calefaccion, asi como radiadores y similares
ES2098003T3 (es) Procedimiento de proteccion de botellas de gas licuado y botellas protegidas asi obtenidas.
BR0211509A (pt) Folha e processo para a preparação de uma folha para a vedação de pelo menos uma barra de ligação, processo para a vedação de uma barra de ligação, e, circuito elétrico

Legal Events

Date Code Title Description
FG2A Definitive protection

Ref document number: 678317

Country of ref document: ES