Cleaning and liquid contact with solids – Processes – For metallic – siliceous – or calcareous basework – including...
Reexamination Certificate
2000-10-27
2003-09-02
Carrillo, Sharidan (Department: 1746)
Cleaning and liquid contact with solids
Processes
For metallic, siliceous, or calcareous basework, including...
C134S003000, C134S022100, C134S022110, C134S026000, C134S028000, C134S036000, C134S041000, C134S042000, C204S157150, C588S001000
Reexamination Certificate
active
06613153
ABSTRACT:
BACKGROUND OF THE INVENTION
Field of the Invention
The invention relates to a method for reducing the radioactivity of a metal part, in which an oxide layer is removed from the metal part using a decontamination solution.
A method for the chemical decontamination of surfaces of metallic components of nuclear reactor plants is known, for example, from EP 0 355 628 B1. The aim of a method of this type is to eliminate a radioactively contaminated oxide layer from the surface of metallic components. For this purpose, the decontamination solution used may be a solution which contains, for example, oxalic acid or some other carboxylic acid.
During the prolonged operating life of a nuclear power plant, radionuclides accumulate primarily in the oxidic protective layers which are to be found on the surfaces of metallic components. Consequently, for decontamination work during a customary inspection of a nuclear power plant, it is sufficient to remove the oxide layer. To do this, a suitable decontamination solution is selected in such a way that the base metal of the components is not attacked.
This procedure is appropriate for an inspection, since approx. 98% of the radionuclides are to be found in the oxide layer. Only approx. 2% of the radionuclides diffuse into regions close to the surface of the base metal of which the components are formed.
When components of a nuclear power plant are being replaced or when the plant is being shut down, the approx. 2% of the radionuclides which have diffused into the surface region of the base metal cause the metal to be placed in an ultimate storage site even after decontamination.
Since very large amounts of metal are produced, a very large ultimate storage site would be required, and this is uneconomical.
SUMMARY OF THE INVENTION
It is accordingly an object of the invention to provide a method of removing radionuclides from radioactively contaminated metal that overcomes the above-mentioned disadvantages of the prior art methods of this general type, so that this metal can be treated as inactive scrap in the standard materials circuit.
With the foregoing and other objects in view, there is provided, according to the invention, a method for reducing the radioactivity of a metal part, which comprises removing an oxide layer from the metal part using a decontamination solution, removing one or more agents which have an oxidizing action from the decontamination solution, lowering the redox potential of the solution and the corrosion potential of the metal of which the metal part consists, and thereby removing a layer of the metal.
The removal of one or more agents which have an oxidizing action lowers the redox potential in the decontamination solution and also reduces the corrosion potential of the base metal. Consequently, a controlled attack is carried out on the base metal. In the process, a few micrometers of the base metal are removed.
Since the radionuclides which have penetrated into a the metal by diffusion are to be found only in regions of the metal which are close to the surface, the method according to the invention results in the advantage that the radionuclides are separated from the metal by the controlled attack on the base metal. What remains is advantageously scrap metal which can be treated further in the same way as conventional inactive scrap. On the other hand, no more base metal than necessary is removed, so that only a small amount of waste has to be delivered to an ultimate storage site.
Agents which have an oxidizing action and are removed from the decontamination solution include, for example Fe
3+
and/or residual oxygen. The Fe
3+
which has an oxidizing action emanates from the oxide layer which has been separated from the metal surface in a preceding decontamination step.
To remove agents which have an oxidizing action, a reducing agent can be added to the decontamination solution. A reducing agent of this type can be used to convert the disruptive Fe
3+
into Fe
2+
, which does not cause a problem. Such a reducing agent can be, for example, ascorbic acid.
To remove agents which have an oxidizing action and are generally gases, it is also possible to pass an inert gas through the decontamination solution. As a result, the residual oxygen which is still present is expelled. One example of a suitable inert gas is nitrogen.
According to a particularly advantageous refinement of the method, the decontamination solution is irradiated with UV light in order to remove agents which have an oxidizing action. This results in the advantage that both disruptive Fe
3+
and disruptive residual oxygen can be removed with the aid of an organic decontamination acid which, on account of the preceding decontamination step, is still present in the decontamination solution.
Under UV irradiation, Fe
2+
and carbon dioxide are formed from the disruptive Fe
3+
and organic decontamination acid which is present. The Fe
2+
which is formed in this way and organic decontamination acid which is present, together with the disruptive residual oxygen, under UV irradiation then form Fe
3+
and carbon dioxide. This reaction proceeds until there is no longer any oxygen present. The Fe
3+
formed is then converted into Fe
2+
and carbon dioxide according to the first reaction described, so that then only these two substances, and no agents which have an oxidizing action, remain.
By way of example, Fe
2+
ions which form are removed using a cation exchanger. A cation exchanger advantageously has a very high capacity. For this reason, a small ion exchanger is sufficient. In fact, for direct removal of Fe
3+
ions, since Fe
3+
forms organic complexes with organic decontamination acids, for example an oxalate complex, an anion exchanger would be necessary, the capacity of which is considerably lower than that of a cation exchanger. Furthermore, the conversion of Fe
3+
into Fe
2+
has the advantage that the remaining decontamination solution to be disposed of does not contain any chelates (chelate complexes), which would have to be eliminated at high cost.
To improve the removal of base metal, nitric acid may additionally be added to the decontamination solution, for example in a concentration of from 100 ppm to 10, 000 ppm in the solution.
By way of example, the method for removing agents which have an oxidizing action is not continued until there are no longer any agents which have an oxidizing action present. To this end, the removal is stopped, for example through the addition of an oxidizing agent. The oxidizing agent may, for example, be air, oxygen, iron(3) ions, hydrogen peroxide and/or ozone.
Stopping the removal of agents which have an oxidizing action has the advantage that it is possible to remove only a desired, very thin layer from the base metal. This is because it has been found that the radionuclides only penetrate into the base metal down to a depth of a few tens of micrometers by diffusion, i.e. by the exchange of lattice sites in the metal lattice. By way of example, the removal of agents which have an oxidizing action from the decontamination solution is initiated and stopped in an alternating sequence. If the switch from initiation and stopping of the attack on the base metal takes place as quickly as possible, it is particularly advantageously possible to remove only precisely that amount of metal which contains the radionuclides present in the region close to the surface. Advantageously, the treatment time and also the amount of waste which has to be disposed of in an ultimate storage site are greatly minimized. The removal of base metal can be controlled by switching between initiation and stopping in individual steps of up to a tenth of a micrometer. Depending on requirements, it is then possible to remove metal to a few hundreds of micrometers or even less.
The method according to the invention has the particular advantage that radioactively contaminated metal parts, following the treatment, can be recycled as usual as uncontaminated scrap and do n
Bertholdt Horst-Otto
Gassen Rainer
Strohmer Franz
Carrillo Sharidan
Framatome ANP GmbH
Locher Ralph E.
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