Patent Number: 
Section: claims

1. A method for the solidification and stabilization of concentrated aqueous sodium hydroxide solution, wherein the following steps are carried out:a) a hydraulic binder containing blast furnace slag is admixed with said sodium hydroxide solution originating from a nuclear reactor, to form a slurry, andb) the slurry is left to set to a solid product, wherein at least one additional source selected from the group consisting of a calcium ion, a magnesium ion, a silica, or any mixture thereof, is added in step a), and wherein the sodium incorporation rate is greater than or equal to 100 kg/m3 of solidified slurry. 2. The method according to claim 1 wherein, in step (a), the slurry is prepared in the presence of at least one adjuvant selected from the group consisting of a plasticizer, a retarder , and any mixture thereof. 3. The method according to claim 1, wherein the concentration of the sodium hydroxide solution is between 8 N and 18 N. 4. The method according to claim 2, wherein the concentration of the sodium hydroxide solution is between 8 N and 14 N. 5. The method according to claim 2 wherein the adjuvant of the plasticizer or retarder type is used in an amount of 0.05 to 5% by dry weight of adjuvant, based on the dry weight of hydraulic binder. 6. The method according to claim 5, wherein the adjuvant of the plasticizer or retarder type is used in an amount of 0.05 to 2% by dry weight of adjuvant, based on the dry weight of hydraulic binder. 7. The method according to claim 2 wherein the adjuvant of the plasticizer or retarder type is selected from the group consisting of naphthalene sulfonate polymers, melamine/formaldehyde polymers, water-soluble acrylic polymers, polyoxyethylene-polycarboxylate polymers, and setting retarders selected from a lignosulfonate setting retarder , a gluconate- setting retarder, and any mixture thereof. 8. The method according to claim 7, wherein the adjuvant of the plasticizer or retarder type is based on sodium gluconate. 9. The method according to claim 1, wherein the calcium or magnesium source is selected from the group consisting of nitrate, sulfate, chloride and carbonate salts of calcium or magnesium. 10. The method according to claim 9, wherein the calcium source is selected from the group consisting of a calcium-rich thermal power station ash, sulfo-calcium ash, anhydrite (calcium sulfate), ground dolomite (CaMg(CO3)2) ground calcite (calcium carbonate), and any mixture thereof. 11. The method according to claim 10, wherein the magnesium source is ground dolomite (CaMg(CO3)2). 12. The method according to claim 9, wherein the calcium source comprises calcium sulfate and the concentration of the sodium hydroxide solution is between 14 N and 18 N. 13. The method according to claim 12, wherein the calcium source is anhydrite. 14. The method according to claim 1 , wherein the ratio of the amount of calcium and/or magnesium in the slurry to the amount of sodium (mol/mol) is between 0.01 and 0.6. 15. The method according to claim 1, wherein the ratio of the amount of hydraulic binder containing blast furnace slag to the amount of aqueous sodium hydroxide solution (weight/weight) is between 0.3 and 2. 16. The method according to claim 1, wherein the ratio of the amount of hydraulic binder containing blast furnace slag to the amount of aqueous sodium hydroxide solution (weight/weight) is between 0.4 and 1.5. 17. The method according to claim 1, wherein the hydraulic binder is selected from the group consisting of a blast furnace slag cement (CEM III A, B or C) and ground pure slag. 18. The method according to claim 17, wherein the hydraulic binder comprises particles with a size predominantly below 200 μm. 19. The method according to claim 17, wherein the hydraulic binder comprises particles with a size predominantly below 100 μm. 20. The method according to claim 1, wherein said slurry contains a source of silica selected from the group consisting of ground silica, thermal power station silico-aluminous fly ash, fluidized bed ash, and any mixture thereof. 21. The method according to claim 20, wherein the amount of ash is between 25 kg and 500 kg per m3 of slurry. 22. The method according to claim 20, wherein the amount of ash is between 50 kg and 350 kg per m3 of slurry. 23. The method according to claim 1, wherein said slurry is packaged in a container that can be used as storage means.