Patent Number: 
Section: claims

1. A method of volumetric oxidative treatment of spent nuclear fuel (SNF) of uranium dioxide, the method comprising thermal processing a reaction mass of SNF element fragments in oxidative environment, said thermal processing being carried out in at least one reaction chamber in two phases, the first phase being performed at 400-650° C. for 60-360 minutes in the gas stream of air additionally comprising carbon dioxide in the amount of 1-4 volume %, the second phase being performed at 350-450° C. for 30-120 minutes in the gas stream of air that includes water steam in the amount corresponding to the dew point of gas-vapor mixture at 30-40° C., the both phases being performed with a repeated mechanical activation of the reaction mass. 2. The method according to claim 1, wherein an hourly rate of the gas stream at said first and second phases is about 10-50 full exchanges of a reaction chamber volume at each phase. 3. The method according to claim 1, further providing preheating the gas stream up to an internal temperature of the at least one reaction chamber before the gas stream enters the at least one reaction chamber at said first phase and second phase, respectively. 4. The method according to claim 1, wherein the gas stream of air at the second phase is oxygen enriched. 5. The method according to claim 1, wherein the at least one reaction chamber includes two reaction chambers, the first phase being carried out in one of the two reaction chambers, the second phase being carried out in another of the two reaction chambers. 6. A method of volumetric oxidative treatment of spent nuclear fuel (SNF) of uranium dioxide, the method comprising thermal processing a reaction mass of SNF element fragments in oxidative environment, said thermal processing being carried out in at least one reaction chamber in two phases, the first phase being performed at 400-650° C. for 60-360 minutes in the gas stream of air additionally comprising carbon dioxide in the amount of 1-4 volume %, the second phase being performed at 350-450° C. for 30-120 minutes in the gas stream of air that includes water steam in the amount corresponding to the dew point of gas-vapor mixture at 30-40° C., an hourly rate of the gas stream being about 10-50 full exchanges of the at least one reaction chamber volume at each phase, the both phases being performed with a repeated mechanical activation of the reaction mass. 7. The method according to claim 6, further providing preheating the gas stream up to an internal temperature of the at least one reaction chamber before the gas stream enters the at least one reaction chamber at said first phase and second phase, respectively. 8. The method according to claim 6, wherein the gas stream of air at the second phase is oxygen enriched. 9. The method according to claim 6, wherein the at least one reaction chamber includes two reaction chambers, the first phase being carried out in one of the two reaction chambers, the second phase being carried out in another of the two reaction chambers. 10. A method of volumetric oxidative treatment of spent nuclear fuel (SNF) of uranium dioxide, the method comprising thermal processing a reaction mass of SNF element fragments in oxidative environment, said thermal processing being carried out in a reaction chamber in two phases, the first phase being performed at 400-650° C. for 60-360 minutes in the gas stream of air additionally comprising carbon dioxide in the amount of 1-4 volume %, the second phase being performed at 350-450° C. for 30-120 minutes in the gas stream of air that includes water steam in the amount corresponding to the dew point of gas-vapor mixture at 30-40° C., the both phases being performed with a repeated mechanical activation of the reaction mass, the gas stream being preheated up to an internal temperature of the reaction chamber before the gas stream is used at said first phase and second phase. 11. The method according to claim 10, wherein the gas stream of air at the second phase is oxygen enriched. 12. The method according to claim 10, wherein an hourly rate of the gas stream is about 10-50 full exchanges of the reaction chamber volume at each phase. 13. The method according to claim 10, wherein the reaction chamber includes a first and a second reaction chambers, the first phase being carried out in the first reaction chamber and the second phase being carried out in the second reaction chamber.