Method for cryogenic separation of air, and air separation plant

Abstract Method for cryogenic separation of air, and air separation plant A method for cryogenic separation of air using an air separation plant (100 - 900) is proposed, wherein, in a mass transfer column (13), a liquid first fluid and a gaseous 5 second fluid are subjected to mass transfer with one...

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description Abstract Method for cryogenic separation of air, and air separation plant A method for cryogenic separation of air using an air separation plant (100 - 900) is proposed, wherein, in a mass transfer column (13), a liquid first fluid and a gaseous 5 second fluid are subjected to mass transfer with one another, wherein a gaseous third fluid is removed from the mass transfer column (13) and is at least partly discharged from the air separation plant (100 - 900), wherein a liquid fourth fluid is removed from the mass transfer column (13) and is at least partly fed into a low-pressure column (12), and wherein the first fluid is formed using at least a part of an oxygen-rich liquid 10 removed from the low-pressure column (12). The second fluid is formed using an oxygen-enriched liquid removed from a high-pressure column (11). The oxygen enriched liquid removed from the high-pressure column (11) and bottom liquid of the mass transfer column (13) are mixed and, by means of a condenser-evaporator (7), partly evaporated, in which condenser-evaporator a liquid stream which comprises at 15 least a part of the oxygen-enriched liquid removed from the high-pressure column (11) and at least a part of the bottom liquid from the mass transfer column (13) is forced through an evaporation space by means of its own pressure and partly evaporated therein. A liquid fifth fluid is removed from the mass transfer column (13) between a feed point for the first fluid and a feed point for the oxygen-enriched liquid, and is at 20 least partly fed into the low-pressure column (12), wherein the fifth fluid or the fraction thereof fed into the low-pressure column (12) is fed into the low-pressure column (12) below the fourth fluid or the fraction thereof fed into the low-pressure column (12). The invention also relates to an air separation plant (100 - 900). 25 (Figure 1) 'I'l Em C)O -~CD t ®r * T * ~ /~~C4 Ca ce/
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The second fluid is formed using an oxygen-enriched liquid removed from a high-pressure column (11). The oxygen enriched liquid removed from the high-pressure column (11) and bottom liquid of the mass transfer column (13) are mixed and, by means of a condenser-evaporator (7), partly evaporated, in which condenser-evaporator a liquid stream which comprises at 15 least a part of the oxygen-enriched liquid removed from the high-pressure column (11) and at least a part of the bottom liquid from the mass transfer column (13) is forced through an evaporation space by means of its own pressure and partly evaporated therein. A liquid fifth fluid is removed from the mass transfer column (13) between a feed point for the first fluid and a feed point for the oxygen-enriched liquid, and is at 20 least partly fed into the low-pressure column (12), wherein the fifth fluid or the fraction thereof fed into the low-pressure column (12) is fed into the low-pressure column (12) below the fourth fluid or the fraction thereof fed into the low-pressure column (12). 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The second fluid is formed using an oxygen-enriched liquid removed from a high-pressure column (11). The oxygen enriched liquid removed from the high-pressure column (11) and bottom liquid of the mass transfer column (13) are mixed and, by means of a condenser-evaporator (7), partly evaporated, in which condenser-evaporator a liquid stream which comprises at 15 least a part of the oxygen-enriched liquid removed from the high-pressure column (11) and at least a part of the bottom liquid from the mass transfer column (13) is forced through an evaporation space by means of its own pressure and partly evaporated therein. A liquid fifth fluid is removed from the mass transfer column (13) between a feed point for the first fluid and a feed point for the oxygen-enriched liquid, and is at 20 least partly fed into the low-pressure column (12), wherein the fifth fluid or the fraction thereof fed into the low-pressure column (12) is fed into the low-pressure column (12) below the fourth fluid or the fraction thereof fed into the low-pressure column (12). 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The second fluid is formed using an oxygen-enriched liquid removed from a high-pressure column (11). The oxygen enriched liquid removed from the high-pressure column (11) and bottom liquid of the mass transfer column (13) are mixed and, by means of a condenser-evaporator (7), partly evaporated, in which condenser-evaporator a liquid stream which comprises at 15 least a part of the oxygen-enriched liquid removed from the high-pressure column (11) and at least a part of the bottom liquid from the mass transfer column (13) is forced through an evaporation space by means of its own pressure and partly evaporated therein. A liquid fifth fluid is removed from the mass transfer column (13) between a feed point for the first fluid and a feed point for the oxygen-enriched liquid, and is at 20 least partly fed into the low-pressure column (12), wherein the fifth fluid or the fraction thereof fed into the low-pressure column (12) is fed into the low-pressure column (12) below the fourth fluid or the fraction thereof fed into the low-pressure column (12). The invention also relates to an air separation plant (100 - 900). 25 (Figure 1) 'I'l Em C)O -~CD t ®r * T * ~ /~~C4 Ca ce/</abstract><oa>free_for_read</oa></addata></record>
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subjects BLASTING
COMBINED HEATING AND REFRIGERATION SYSTEMS
HEAT PUMP SYSTEMS
HEATING
LIGHTING
LIQUEFACTION SOLIDIFICATION OF GASES
LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS
MANUFACTURE OR STORAGE OF ICE
MECHANICAL ENGINEERING
MIXTURES BY PRESSURE AND COLD TREATMENT
REFRIGERATION OR COOLING
WEAPONS
title Method for cryogenic separation of air, and air separation plant
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