Method for the surface decontamination of component parts of the coolant cycle of a nuclear reactor
US-2015364226-A1 · Dec 17, 2015 · US
US10950360B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10950360-B2 |
| Application number | US-201716085072-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 1, 2017 |
| Priority date | Mar 16, 2016 |
| Publication date | Mar 16, 2021 |
| Grant date | Mar 16, 2021 |
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A method for treating waste water from the decontamination of a metal surface in a primary coolant circuit of a nuclear reactor comprises discharging a predetermined amount of an oxidation solution from the primary coolant circuit into a reduction zone connected to the primary coolant circuit and reacting the oxidation solution with a reducing agent to form a reaction solution that is freed of oxidizing agent, and passing the reaction solution over an ion-exchange resin in order to form a desalinated solution, and returning the desalinated solution to the primary coolant and/or disposing of the desalinated solution. A waste water treatment apparatus for carrying out the method is also provided.
Opening claim text (preview).
The invention claimed is: 1. A waste water treatment apparatus for treating waste water from decontamination of a metal surface in a primary coolant circuit of a nuclear reactor, said apparatus comprising: a discharge device provided for discharging a predetermined amount of a primary coolant comprising an oxidizing agent from the primary coolant circuit, a reduction zone that is connected to the discharge device and comprises a dosing station for introducing a reducing agent into the predetermined amount of the primary coolant discharged from the primary coolant circuit, and which reduction zone is provided for the reaction of the reducing agent with the oxidizing agent in the primary coolant to form a reaction solution, and an ion exchanger connected to the reduction zone for deionizing the reaction solution. 2. The waste water treatment apparatus according to claim 1 , characterized in that the primary coolant circuit comprises at least one coolant pump with a seal water supply. 3. The waste water treatment apparatus according to claim 1 , characterized in that the reduction zone comprises a reaction vessel. 4. The waste water treatment apparatus according to claim 3 , characterized in that the reaction vessel is a stirred-tank reactor. 5. The waste water treatment apparatus according to claim 4 , characterized in that the reduction zone further comprises a buffer vessel connected to the stirred-tank reactor. 6. The waste water treatment apparatus according to claim 3 , characterized in that the reaction vessel comprises a tubular-flow reactor. 7. The waste water treatment apparatus according to claim 6 , characterized in that the tubular-flow reactor has a length such that a residence time of the reaction solution in the tubular-flow reactor is achieved in which the oxidizing agent essentially completely reacts with the reducing agent. 8. The waste water treatment apparatus according to claim 1 , characterized in that the nuclear reactor is constructed as a pressurized-water reactor, a boiling-water reactor or a heavy-water reactor. 9. A method for treating waste water from decontamination of a metal surface in a primary coolant circuit of a nuclear reactor with a waste water treatment apparatus according to claim 1 , characterized in that the method comprises steps for: a) introducing an oxidizing agent into the primary coolant in the primary coolant circuit to form an oxidation solution, and circulating the oxidation solution in the primary coolant circuit to contact the oxidation solution with the metal surface; b) during or after step a), discharging a predetermined amount of the oxidation solution from the primary coolant circuit into the reduction zone connected to the primary coolant circuit; c) in the reduction zone, reacting the oxidizing agent with a reducing agent to form a reaction solution freed of the oxidizing agent; d) passing the reaction solution over an ion exchange resin in the ion exchanger to form a desalinated solution; and e) returning the desalinated solution to the primary coolant and/or temporarily storing and/or disposing of the desalinated solution. 10. The method of claim 9 , characterized in that the oxidizing agent is a permanganate. 11. The method according to claim 9 , characterized in that the reducing agent is an aliphatic dicarboxylic acid. 12. The method according to claim 9 , characterized in that the primary coolant circuit comprises at least one coolant pump with a seal water supply, and that the oxidation solution is circulated in the primary coolant circuit using the coolant pump. 13. The method according to claim 12 , characterized in that seal water is fed to the coolant pump and delivered into the primary coolant, wherein the predetermined amount of oxidation solution discharged from the primary coolant circuit corresponds to the amount of seal water delivered into the primary coolant. 14. The method according to claim 12 , characterized in that a volumetric flow rate of the oxidation solution discharged into the reduction zone corresponds to a volumetric flow rate of the seal water delivered into the primary coolant during step a). 15. The method according to claim 9 , characterized in that the reaction solution has a residence time in the reduction zone that is adapted to a reaction time of the reaction of the oxidizing agent with the reducing agent to achieve an essentially complete reaction of the oxidizing agent with the reducing agent in the reduction zone. 16. The method according to claim 9 , characterized in that the reduction zone comprises a tubular-flow reactor, wherein the oxidizing agent and the reducing agent have a residence time in the tubular-flow reactor that is controlled to achieve an essentially complete reaction of the oxidizing agent with the reducing agent in the tubular-flow reactor. 17. The method according to claim 9 , characterized in that the reduction zone is pressurized if required to prevent outgassing of carbon dioxide. 18. The method according to claim 9 for treating waste water from decontamination of a metal surface in a primary coolant circuit of a nuclear reactor, said method comprising: a) introducing an oxidizing agent into a primary coolant in the primary coolant circuit to form an oxidation solution and circulating the oxidation solution in the primary coolant circuit to contact the oxidation solution with the metal surface; b) during or after step a), discharging a predetermined amount of the oxidation solution through a discharge device of a waste water treatment apparatus, wherein said apparatus comprises said discharge device, a reduction zone connected to the discharge device, said reduction zone comprising a dosing station for introducing a reducing agent into the reduction zone, and an ion exchanger connected to the reduction zone for deionizing the reaction solution, c) reacting in the reduction zone the oxidizing agent with a reducing agent to form a reaction solution freed of the oxidizing agent; d) passing the reaction solution over an ion-exchange resin to form a desalinated solution; and e) returning the desalinated solution to the primary coolant and/or temporarily storing and/or disposing of the desalinated solution. 19. The method according to claim 18 for decontamination of a metal surface in a primary coolant circuit of a nuclear reactor having a layer including one or more metal oxides and radioisotopes, wherein the method comprises one or more treatment cycles, each treatment cycle comprising: an oxidation step in which an oxidizing agent is introduced into a primary coolant in the primary coolant circuit to form an oxidation solution, which oxidation solution is circulated in the primary coolant circuit to contact the oxidation solution with the metal surface; a reduction step in which a reducing agent is introduced into the oxidation solution and the oxidizing agent in the oxidation solution is reduced; and a decontamination step, wherein the metal surface treated in the oxidation step is contacted with a decontaminating agent to dissolve at least a part of the metal oxides and radioisotopes in the primary coolant to form a decontamination solution, wherein a predetermined amount of the oxidation solution formed in the oxidation step is discharged into the waste water treatment apparatus.
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