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US20080271481A1 - Air Separating Device by Means of Cryogenic Distillation - Google Patents

Air Separating Device by Means of Cryogenic Distillation Download PDF

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Publication number
US20080271481A1
US20080271481A1 US12/097,641 US9764106A US2008271481A1 US 20080271481 A1 US20080271481 A1 US 20080271481A1 US 9764106 A US9764106 A US 9764106A US 2008271481 A1 US2008271481 A1 US 2008271481A1
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section
exchange
air
column
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US12/097,641
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Benoit Davidian
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LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
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Assigned to L'AIR LIQUIDE, SOCIETE ANONYME POUR L'ETUDE ET L'EXPLOITATION DES PROCEDES GEORGES CLAUDE reassignment L'AIR LIQUIDE, SOCIETE ANONYME POUR L'ETUDE ET L'EXPLOITATION DES PROCEDES GEORGES CLAUDE ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: DAVIDIAN, BENOIT
Publication of US20080271481A1 publication Critical patent/US20080271481A1/en
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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
    • F25J3/04624—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 integrated mass and heat exchange, so-called non-adiabatic rectification, e.g. dephlegmator, reflux exchanger
    • 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
    • F25J3/04254—Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using the cold stored in external cryogenic fluids
    • 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
    • F25J3/04248—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
    • F25J3/04296—Claude expansion, i.e. expanded into the main or 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
    • F25J3/04866—Construction and layout of air fractionation equipments, e.g. valves, machines
    • F25J3/04872—Vertical layout of cold equipments within in the cold box, e.g. columns, heat exchangers etc.
    • 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
    • F25J5/00—Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants
    • F25J5/002—Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants for continuously recuperating cold, i.e. in a so-called recuperative heat exchanger
    • F25J5/007—Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants for continuously recuperating cold, i.e. in a so-called recuperative heat exchanger combined with mass exchange, i.e. in a so-called dephlegmator
    • 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
    • F25J2200/02—Processes or apparatus using separation by rectification in a single 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
    • F25J2210/00—Processes characterised by the type or other details of the feed stream
    • F25J2210/42—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
    • F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
    • F25J2290/44—Particular materials used, e.g. copper, steel or alloys thereof or surface treatments used, e.g. enhanced surface

Definitions

  • the present invention relates to an apparatus for separating air by cryogenic distillations in particular for producing nitrogen.
  • a nitrogen generator described in U.S. Pat. No. 5,899,093 comprises an exchange line in which the air to be distilled is cooled, a distillation column in which the air is separated into a nitrogen-rich stream at the top of the column and an oxygen-enriched stream at the bottom of the column.
  • a vaporizer-condenser To supply reflux, part of the nitrogen-rich stream is sent to a vaporizer-condenser where it is condensed by heat exchange with the oxygen-enriched stream.
  • the nitrogen may be condensed in a deflegmator.
  • the enriched liquid partially vaporized in the deflegmator is sent to a phase separator and the liquid formed in the separator again flows to the deflegmator. It is an object of the present invention to eliminate the condenser-vaporizer, which imposes various constraints:
  • an apparatus for separating air by cryogenic distillation for producing nitrogen comprising:
  • the exchange line comprises two sections, a deflegmation section and a heat exchange section; the deflegmation section is connected to the column and to the oxygen-enriched liquid line and the heat exchange section is connected to the air supply line and to the deflegmation section.
  • it provides a method for separating air by cryogenic distillation for producing nitrogen in an apparatus comprising an exchange line and a simple distillation column containing plates and/or structured packings, in which compressed and purified air is sent to the exchange line, compressed, purified and cooled air is sent from the exchange line to the distillation column, a stream of oxygen-enriched liquid is withdrawn from the column and sent to the exchange line,
  • the exchange line comprises two sections, a deflegmation section and a heat exchange section; the deflegmation section is connected to the column and to the oxygen-enriched liquid line and the heat exchange section is connected to the air supply line and to the deflegmation section, and in that the oxygen-enriched liquid is vaporized completely in the heat exchange section to produce an oxygen-enriched gas.
  • the invention proposes to incorporate the “vaporization-condensation” function in the main heat exchanger by using the coldest part of the heat exchanger as a deflegmator in order to condense the nitrogen therein.
  • the cold box is higher, but much narrower because the heat exchanger is above the column, thereby procuring a considerable gain.
  • FIGURE shows an air separation apparatus according to the invention.
  • a stream of compressed air is purified in a purification unit (not shown) and sent to the hot end of an exchange line 3 .
  • the exchange line comprises a conventional heat exchange section 3 A and a deflegmation section 3 B.
  • the two sections are contiguous and the exchange line is a plate and brazed fin-tube heat exchanger.
  • the air 1 is cooled in the exchange line up to the cold end of the section 3 A and then exits the exchange line to be sent to the bottom of a simple distillation column 7 .
  • the column 7 contains structured packings or plates 9 .
  • the air is separated into an oxygen-enriched stream 11 and a nitrogen-enriched stream.
  • the oxygen-enriched stream 11 is withdrawn in liquid form from the column 7 and sent to the cold end of the section 3 B.
  • the nitrogen-enriched stream leaves the top of the column directly via the passages of the section 3 B.
  • the exchange line 3 has the same width as the top of the column 7 and is welded to the shell of the column (by a round-square or a round-rectangular adaptor).
  • the cooling capacity required for distillation is supplied by injection feeding of liquid nitrogen 13 , obtained from a storage unit in a manner known per se described in EP-A-0452177.
  • an air turbine 1 or a vaporized enriched liquid turbine may be provided.
  • the section 3 B comprises two nitrogen passages for one passage of enriched liquid.
  • the enriched liquid is completely vaporized in the section 3 B of the exchange line 3 so that it is completely converted to gas.
  • the nitrogen is partly condensed: the condensed part falls by gravity into the column to serve as reflux, the exchange line 3 being installed above the column (by direct welding or optionally via appropriate piping). The remainder of the nitrogen gas continues to rise through the entire exchange line 3 .
  • the section 3 A of the exchange line comprises the conventional main exchange line.
  • the nitrogen gas and vaporized enriched liquid are heated by the incoming air 1 .
  • the double nitrogen passages of the deflegmation section 3 B may be reallocated between the nitrogen to be heated and the air to be cooled in the section 3 A, This can be carried out by fluid inlet/outlet (distribution box), or, preferably, by internal redistribution (use of rods and perforated separating plates).
  • the exchange line 3 is preferably made from copper or aluminum and the column 7 is made from stainless steel. If the exchange line is made from aluminum and the column is made from stainless steel, one or more composite junctions must be provided between the two. If not, the exchange line 3 and the column 7 may be made from aluminum.

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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)

Abstract

The invention relates to an air separating device by means of cryogenic distillation for producing nitrogen, comprising an exchange line (3), a simple distillation column (7) containing plates and/or structured packings, a supply line for delivery of compressed purified air (1) to the exchange line, a supply line for delivery of the compressed purified and cooled air from the exchange line to the distillation column, a line for withdrawal of a liquid (11) enriched in oxygen from the distillation column for delivery to the exchange line, said exchange line having two sections, a rectifying section (3B) and a heat exchange section (3A), the rectifying section being connected to the column and the line for the enriched liquid and the heat exchange section is connected to the air supply line and the rectifying section.

Description

  • The present invention relates to an apparatus for separating air by cryogenic distillations in particular for producing nitrogen.
  • A nitrogen generator described in U.S. Pat. No. 5,899,093 comprises an exchange line in which the air to be distilled is cooled, a distillation column in which the air is separated into a nitrogen-rich stream at the top of the column and an oxygen-enriched stream at the bottom of the column. To supply reflux, part of the nitrogen-rich stream is sent to a vaporizer-condenser where it is condensed by heat exchange with the oxygen-enriched stream. Alternatively, the nitrogen may be condensed in a deflegmator. The enriched liquid partially vaporized in the deflegmator is sent to a phase separator and the liquid formed in the separator again flows to the deflegmator. It is an object of the present invention to eliminate the condenser-vaporizer, which imposes various constraints:
      • investment cost, particularly to provide for liquid recirculation
      • concentration of impurities (CnHm, N2O, CO2, etc.)
      • liquid purge
      • level metering.
  • According to one object of the invention, it provides an apparatus for separating air by cryogenic distillation for producing nitrogen comprising:
      • a) an exchange line
      • b) a simple distillation column containing plates and/or structured packings
      • c) a line for sending compressed and purified air to the exchange line
      • d) a line for sending compressed, purified and cooled air from the exchange line to the distillation column
      • e) a line for withdrawing an oxygen enriched liquid from the column and for sending it to the exchange line
  • characterized in that the exchange line comprises two sections, a deflegmation section and a heat exchange section; the deflegmation section is connected to the column and to the oxygen-enriched liquid line and the heat exchange section is connected to the air supply line and to the deflegmation section.
  • According to optional objects:
      • the exchange line is positioned above the distillation column;
      • the deflegmation section is fixed to the top of the column;
      • means for injection feeding and/or for expanding air or vaporized enriched liquid;
      • the line for sending compressed, purified and cooled air from the exchange line to the distillation column is connected to the cold end of the heat exchange section;
      • means for redistributing the passages between the heat exchange section and the deflegmation section;
      • the exchange line is made from copper or aluminum and/or the distillation column is made from stainless steel;
      • the exchange line and the distillation column are made from aluminum;
      • the exchange line is a plate and brazed fin-tube heat exchanger.
  • According to another aspect of the invention, it provides a method for separating air by cryogenic distillation for producing nitrogen in an apparatus comprising an exchange line and a simple distillation column containing plates and/or structured packings, in which compressed and purified air is sent to the exchange line, compressed, purified and cooled air is sent from the exchange line to the distillation column, a stream of oxygen-enriched liquid is withdrawn from the column and sent to the exchange line,
  • characterized in that the exchange line comprises two sections, a deflegmation section and a heat exchange section; the deflegmation section is connected to the column and to the oxygen-enriched liquid line and the heat exchange section is connected to the air supply line and to the deflegmation section, and in that the oxygen-enriched liquid is vaporized completely in the heat exchange section to produce an oxygen-enriched gas.
  • The invention proposes to incorporate the “vaporization-condensation” function in the main heat exchanger by using the coldest part of the heat exchanger as a deflegmator in order to condense the nitrogen therein. The advantages of the invention are as follows:
      • It provides a “natural” purge of the enriched liquid, which is only slightly concentrated by vaporization (like a pump apparatus).
      • Since there is no need for a deconcentration liquid purge, this serves to:
        • eliminate the equipment associated therewith, including the stone-filled pit (or drip pot) necessary for a regular purge and including the equipment for ensuring the reliability and effectiveness of the purge,
        • a gain in cooling capacity (for an apparatus with injection feeding, the consumption of liquid nitrogen is sharply reduced, thereby reducing the operating cost),
        • alleviate the operational monitoring of this purge which is “critical” in terms of safety.
      • Elimination of level metering, pulse connector heating tongs, optional burners and level gauge, and alleviation of operational monitoring of this measurement which is “critical” in terms of safety.
      • Elimination of the recirculation pot.
  • The extra cost on the heat exchanger is marginal, or even nil, if part of the gain in cooling capacity is converted in a slightly less efficient (and therefore smaller) exchange line.
  • The cold box is higher, but much narrower because the heat exchanger is above the column, thereby procuring a considerable gain.
  • The invention is described in greater detail with reference to the FIGURE, which shows an air separation apparatus according to the invention.
    •
  • A stream of compressed air is purified in a purification unit (not shown) and sent to the hot end of an exchange line 3. The exchange line comprises a conventional heat exchange section 3A and a deflegmation section 3B. The two sections are contiguous and the exchange line is a plate and brazed fin-tube heat exchanger.
  • The air 1 is cooled in the exchange line up to the cold end of the section 3A and then exits the exchange line to be sent to the bottom of a simple distillation column 7. The column 7 contains structured packings or plates 9.
  • The air is separated into an oxygen-enriched stream 11 and a nitrogen-enriched stream. The oxygen-enriched stream 11 is withdrawn in liquid form from the column 7 and sent to the cold end of the section 3B. The nitrogen-enriched stream leaves the top of the column directly via the passages of the section 3B. Preferably the exchange line 3 has the same width as the top of the column 7 and is welded to the shell of the column (by a round-square or a round-rectangular adaptor).
  • The cooling capacity required for distillation is supplied by injection feeding of liquid nitrogen 13, obtained from a storage unit in a manner known per se described in EP-A-0452177. Alternatively or additionally, an air turbine 1 or a vaporized enriched liquid turbine may be provided.
  • The section 3B comprises two nitrogen passages for one passage of enriched liquid. The enriched liquid is completely vaporized in the section 3B of the exchange line 3 so that it is completely converted to gas. The nitrogen is partly condensed: the condensed part falls by gravity into the column to serve as reflux, the exchange line 3 being installed above the column (by direct welding or optionally via appropriate piping). The remainder of the nitrogen gas continues to rise through the entire exchange line 3.
  • The section 3A of the exchange line comprises the conventional main exchange line. The nitrogen gas and vaporized enriched liquid are heated by the incoming air 1.
  • To optimize the exchange line 3, at the interface between the two sections, the double nitrogen passages of the deflegmation section 3B may be reallocated between the nitrogen to be heated and the air to be cooled in the section 3A, This can be carried out by fluid inlet/outlet (distribution box), or, preferably, by internal redistribution (use of rods and perforated separating plates).
  • The exchange line 3 is preferably made from copper or aluminum and the column 7 is made from stainless steel. If the exchange line is made from aluminum and the column is made from stainless steel, one or more composite junctions must be provided between the two. If not, the exchange line 3 and the column 7 may be made from aluminum.

Claims (10)

1-9. (canceled)
10: An apparatus for separating air by cryogenic distillation for producing nitrogen comprising:
a) an exchange line;
b) a simple distillation column containing plates and/or structured packings;
c) a line for sending compressed and purified air to the exchange line;
d) a line for sending compressed, purified and cooled air from the exchange line to the distillation column; and
e) a line for withdrawing an oxygen-enriched liquid from the column and for sending it to the exchange line,
wherein the exchange line comprises two sections, a deflegmation section and a heat exchange section; the deflegmation section is connected to the column and to the oxygen-enriched liquid line and the heat exchange section is connected to the air supply line and to the deflegmation section.
11: The apparatus of claim 10, in which the exchange line is positioned above the distillation column.
12: The apparatus of claim 10, in which the deflegmation section is fixed to the top of the column.
13: The apparatus of claim 10, comprising means for injection feeding and/or for expanding air or vaporized enriched liquid.
14: The apparatus of claim 10, in which the line for sending compressed, purified, and cooled air from the exchange line to the distillation column is connected to the cold end of the heat exchange section.
15: The apparatus of claim 10, comprising means for redistributing the passages between the heat exchange section and the deflegmation section.
16: The apparatus of claim 10, in which the exchange line is made from copper or aluminum and/or the distillation column is made from stainless steel.
17: The apparatus of claim 10, in which the exchange line and the distillation column are made from aluminum.
18: A method for separating air by cryogenic distillation for producing nitrogen in an apparatus comprising an exchange line and a simple distillation column containing plates and/or structured packings, in which compressed and purified air is sent to the exchange line, compressed, purified and cooled air is sent from the exchange line to the distillation column, a stream of oxygen-enriched liquid is withdrawn from the column and sent to the exchange line, wherein the exchange line comprises two sections, a deflegmation section and a heat exchange section; the deflegmation section is connected to the column and to the oxygen-enriched liquid line and the heat exchange section is connected to the air supply line and to the deflegmation section, and in that the oxygen-enriched liquid is vaporized completely in the heat exchange section to produce an oxygen-enriched gas.
US12/097,641 2005-12-20 2006-12-15 Air Separating Device by Means of Cryogenic Distillation Abandoned US20080271481A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
FR0553971A FR2895069B1 (en) 2005-12-20 2005-12-20 APPARATUS FOR AIR SEPARATION BY CRYOGENIC DISTILLATION
FR0553971 2005-12-20
PCT/FR2006/051366 WO2007074276A2 (en) 2005-12-20 2006-12-15 Air separating device by means of cryogenic distillation

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US20080271481A1 true US20080271481A1 (en) 2008-11-06

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US (1) US20080271481A1 (en)
EP (1) EP1966554B1 (en)
JP (1) JP5074416B2 (en)
CN (1) CN101341370B (en)
DK (1) DK1966554T3 (en)
ES (1) ES2689041T3 (en)
FR (1) FR2895069B1 (en)
PL (1) PL1966554T3 (en)
WO (1) WO2007074276A2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2026025A1 (en) * 2007-07-30 2009-02-18 Linde Aktiengesellschaft Process and device for producing high pressure nitrogen by cryogenic separation of air in a single column
FR2929384A1 (en) * 2008-03-27 2009-10-02 Air Liquide Air separating apparatus, has distillation column comprising head condenser with dephlegmator whose horizontal section covers seventy percentage of section of column, and extracting unit extracting nitrogen enriched product in column head
WO2009063146A1 (en) * 2008-03-28 2009-05-22 L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Heat exchanger and cryogenic-distillation-based air separation device including one such exchanger
FR2973486B1 (en) * 2011-03-31 2013-05-03 Air Liquide AIR SEPARATION METHOD BY CRYOGENIC DISTILLATION
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DK1966554T3 (en) 2018-10-15
FR2895069A1 (en) 2007-06-22

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