Patent Number: 042773636
Section: claims

1. A method for processing a mixture of air and rare gases, at least some portion of which is radioactive, as gaseous effluents arising from the reprocessing of irradiated fuels, wherein said method comprises concentrating the rare gases in solution in liquid argon, as a liquefied mixture, by cryogenic distillation of light gases, a major portion of which is nitrogen, from the liquefied mixture. 2. A method according to claim 1, wherein said method comprises a cryogenic distillation from the concentrated and liquefied mixture to recover xenon. 3. A method according to claim 1, wherein the concentration of the rare gases is carried out at a maximum pressure of 18 bar. 4. A method for processing effluent gases arising from the reprocessing of irradiated nuclear fuels and comprising a mixture of gases containing at least radioactive krypton and xenon in air, wherein said method successively comprises (1) removing any impurities from said mixture,  (2) concentrating xenon and krypton in solution in liquid argon as a liquefied mixture by distillation of light gases, a major portion of which is nitrogen, from the liquefied mixture,  (3) liquefying the mixture of argon, xenon and krypton separated in step (2) and removing argon therefrom by cryogenic distillation thereof to obtain a mixture remaining of xenon and krypton, and  (4) liquefying the mixture of xenon and krypton obtained in step (3) and separating the xenon from the krypton by cryogenic distillation thereof. 5. A method according to claim 4, wherein part of the krypton which has been separated from the xenon and obtained during step (4) is introduced into the mixture obtained at the end of step (1) before proceeding to the concentration of the xenon and krypton in solution in liquid argon in step (2). 6. A method according to claim 4, wherein step (1) comprising removing any impurities comprises an initial stage of removal of hydrocarbons by catalytic oxidation, a second stage of removal of oxygen and nitrogen oxides by catalytic reduction, and a third stage of removal of carbon dioxide gas and of water vapor by passage through a molecular sieve and/or silica gel. 7. A method according to claim 4, wherein the separation of xenon and krypton in step (4) is carried out at a pressure of approximately 3 bar. 8. A method according to claim 4, wherein the removing of argon from the mixture of argon, xenon and krypton in step (3) is carried out at a pressure between the pressure at which step (4) is conducted and the pressure at which step (2) is conducted.