Patent Number: 056334230
Section: claims

1. A process for decontamination of radioactive liquid effluents, comprising the steps of placing a consumable anode and a cathode in the liquid effluent in a reactor, bringing the pH of the effluent to a value equal to or above 1, and establishing a direct current between the electrodes while maintaining the potential of the anode at a value equal to or above 2 V/NHE until the consumed electricity quantity is equal to or above 8 coulombs/milliliter, wherein said consumable anode is constituted by a metal alloy comprising between 20 and 70 wt. % iron, between 20 and 40 wt. % cobalt and between 5 and 30 wt. % aluminum, the total sum of the weight percentages of these three elements being equal to or below 100. 2. A process according to claim 1, wherein the step of establishing a direct current between the electrodes includes maintaining the potential of the anode at substantially 5.0 V/NHE. 3. A process according to claim 1 or 2, including the further steps of extracting the sludge formed in the reactor, reinjecting into said reactor a part of the extracted sludge, and separating the remaining part of the extracted sludge by solid/liquid separation. 4. A process according to claim 1 or 2, wherein said consumable anode also comprises less than 20 wt. % nickel. 5. A process according to claim 1 or 2, wherein consumable anode also comprises less than 10 wt. % titanium. 6. A process according to claim 1 or 2, wherein said consumable anode also comprises less than 5 wt. % copper. 7. A process according to claim 1 or 2, wherein said consumable anode also comprises less than 5 wt. % niobium. 8. A process for decontamination of radioactive liquid effluents, containing antimony, or ruthenium, or strontium, or cesium or actinides, comprising the steps of placing a consumable anode and a cathode in the liquid effluent in a reactor, bringing the pH of the effluent to a value equal to or above 1, and establishing a direct current between the electrodes while maintaining the potential of the anode at a value equal to or above 2 V/NHE, wherein said consumable anode is constituted by a metal alloy comprising between 20 and 70 wt. % iron, between 20 and 40 wt. % cobalt and between 5 and 30 wt. % aluminum, the total sum of the weight percentages of these three elements being equal to or below 100. 9. A process according to claim 8, wherein the step of establishing a direct current between the electrodes includes maintaining the potential of the anode at substantially 5.0 V/NHE. 10. A process according to claim 8 or 9, wherein the step of establishing a direct current between the electrodes includes maintaining the current until the consumed electricity quantity is equal to or above 8 coulombs/milliliter. 11. A process according to claim 8 or 9, including the further steps of extracting the sludge formed in the reactor, reinjecting into said reactor a part of the extracted sludge, and separating the remaining part of the extracted sludge by solid/liquid separation. 12. A process according to claim 8 or 9, wherein said consumable anode also comprises less than 20 wt. % nickel. 13. A process according to claim 8 or 9, wherein consumable anode also comprises less than 10 wt. % titanium. 14. A process according to claim 8 or 9, wherein said consumable anode also comprises less than 5 wt. % copper. 15. A process according to claim 8 or 9, wherein said consumable anode also comprises less than 5 wt. % niobium.