Patent Number: 050733338
Section: claims

1. A method of decontaminating radio nuclide-contaminated corrosion products, which are insoluble or sparingly soluble in acids, from primary systems surfaces in nuclear reactors of the pressurized water type, the boiler reactor type with hydrogen dosage and similar, especially for the decontamination for the purpose of demolishing or scrapping such reactors or components thereof, where the contaminated surfaces are contacted with an oxidation agent in an acid solution so as to obtain an oxidation in the presence of Ce.sup.4+ ions, ozone and chromic acid, and the corrosion products which have been made acid soluble by means of said oxidation are dissolved, characterized by performing said oxidation with Ce.sup.4+ ions, ozone and chromic acid with concentrations thereof required for said decontamination, in the presence of perhalogen acid at a pH below 3. 2. A method according to claim 1, characterized by performing said oxidation in the presence of Ce.sup.4+ in a concentration of 0.01-50 g/l, ozone in a concentration of 0.001-1 g/l and chromic acid in a concentration of 0.001-50 g/l. 3. A method according to claim 1, characterized by using as said cerium compound cerium perhalogenate perchlorate, or cerium nitrate. 4. A method according to claim 1, characterized by performing said oxidation in the presence of perhalogen acid in such a concentration that the pH value is below 2. 5. A method according to claim 1, characterized by performing said oxidation with perhalogen acid having a molarity within the range of 0.01-8M. 6. A method according to claim 1, characterized by using as said oxidizing agent an acidic aqueous solution of Ce.sup.4+ and chromic acid as well as ozone in a saturated solution and dispersed form. 7. A method according to claim 1, characterized by using as said oxidation agent a two-phase ozone gas-aqueous mixture where ozone in gaseous form has been dispersed in an acidic aqueous solution of Ce.sup.4+ and chromic acid. 8. A method according to claim 1, characterized by performing the oxidation and dissolution in one and the same step. 9. A method according to claim 1, characterized by performing the oxidation and dissolution at a temperature below about 60.degree. C. 10. A method according to claim 1, characterized by performing the oxidation with an external addition of chromic acid to the oxidation solution. 11. A method according to claim 1, characterized by performing said oxidation in the presence of Ce.sup.4+ in a concentration of 0.5-10 g/l, ozone in a concentration of 0.001-0.05 g/l and chromic acid in a concentration of 0.005-0.2 g/l. 12. A method according to claim 2, characterized by using as said cerium compound cerium perhalogenate, or cerium nitrate. 13. A method according to claim 2, characterized by performing said oxidation in the presence of perhalogen acid in such a concentration that the pH value is below 2. 14. A method according to claim 2, characterized by performing said oxidation with perhalogen acid having a molarity within the range of 0.01-8M. 15. A method according to claim 2, characterized by using as said oxidation agent an acidic aqueous solution of Ce.sup.4+ and chromic acid as well as ozone in a saturated solution and dispersed form. 16. A method according to claim 2, characterized by using as said oxidation agent a two-phase ozone gas-aqueous mixture where ozone in gaseous form has been dispersed in an acidic aqueous solution of Ce.sup.4+ and chromic acid. 17. A method according to claim 2, characterized by performing the oxidation and dissolution in one and the same step. 18. A method according to claim 2, characterized by performing the oxidation and dissolution at a temperature below about 60.degree. C. 19. A method according to claim 2, characterized by performing the oxidation with an external addition of chromic acid to the oxidation solution. 20. A method according to claim 2, characterized by performing said oxidation in the presence of Ce.sup.4+ in a concentration of 0.5-10 g/l, ozone in a concentration of 0.001-0.05 g/l and chromic acid in a concentration of 0.005-0.2 g/l. 21. A method according to claim 1 wherein said perhalogen acid is perchloric acid. 22. A method according to claim 3 wherein said cerium perhalogenate is cerium perchlorate. 23. A method according to claim 1 wherein said perhalogen acid is provided in such a concentration that the pH value is below 1. 24. A method according to claim 1 wherein said perhalogen acid is provided in such a concentration that the pH value is within the range of 0.5-1. 25. A method according to claim 1, characterized by performing said oxidation with perhalogen acid having a molarity within the range of 0.1-2M. 26. A method according to claim 9, characterized by performing the oxidation and dissolution at a temperature within the range of 20.degree.-30.degree. C. 27. A method according to claim 9, characterized by performing the oxidation and dissolution at a temperature within the range of 20.degree.-25.degree. C. 28. A method according to claim 2, characterized by using as said cerium compound cerium perchlorate. 29. A method according to claim 2, wherein perhalogen acid is provided in such a concentration that the pH value is below 1. 30. A method according to claim 2, wherein said perhalogen acid is provided in such a concentration that the pH value is within the range of 0.5-1. 31. A method according to claim 2, characterized by performing said oxidation with perhalogen acid having a molarity within the range of 0.1-2M. 32. A method according to claim 2, characterized by performing the oxidation and dissolution at a temperature within the range of 20.degree.-30.degree. C. 33. A method according to claim 2, characterized by performing the oxidation and dissolution at a temperature within the range of 20.degree.-25.degree. C.