| 摘要 |
A stream of compressed air is purified in a unit 4 by removal of carbon dioxide and water vapour. The air is cooled by passage through a heat exchanger 6 to a temperature suitable for its rectification. The air is separated in a higher pressure rectifier 12 into oxygen-enriched liquid and nitrogen vapour. A stream of the oxygen-enriched liquid is reduced in pressure and introduced into a phase separator 42 provided with a reboiler 22 with the result that further separation takes place and a liquid further enriched in oxygen and an intermediate vapour are formed. A stream of the further-enriched liquid is separated into oxygen and nitrogen in a lower pressure rectifier 34. A stream of the intermediate vapour is condensed in a condenser 46 and is introduced into the lower pressure rectifier 34. A part of the liquid nitrogen reflux for the rectifiers 12 and 34 is formed by condensing nitrogen vapour separated in the rectifier 12 by indirect heat exchange with liquid from an intermediate mass transfer region of the rectifier 34. Another part of the liquid nitrogen reflux is formed by vaporising impure oxygen product of the rectifier 34 in a condenser-reboiler 72 by indirect heat exchange with nitrogen vapour taken from the rectifier 34. <IMAGE> |
