IMPROVEMENTS IN OR RELATING TO THE OZONE OXIDATION OF DEPOSITS IN COOLING SYSTEMS OF NUCLEAR REACTORS

Abstract: Process for oxidizing chromium in deposits in the cooling system of a nuclear reactor using a solution of ozone which consists of adding to the solution from 0.01 to 0.5% of a water-soluble cerium IV compound, from 0.1 to 0.5% of a water-soluble aromatic compound having at least one ketone group on an aromatic ring, or adding both. Further a composition of water, ozone, the cerium IV compound and the aromatic compound. Also a process for decontaminating the cooling system of nuclear reactors by adding a decon­ tamination composition to the coolant, circulating the coolant between the cooling system and a cation exchange resin, removing the decontamination composition by pas­ sing it through an anion exchange resin, adjusting the temperature to 40 to 100°C, adding the ozone oxidation composition, circulating the coolant through the cooling system, raising the temperature to at least 100°C, passing the coolant through an anion exchange resin or a mixed resin, adjusting the temperature to frm 60 to 100°C and repeating the addition of the decontamination composition and its removal.

Description: IMPROVEMENTS IN OR RELATING TO THE OZONE OXIDATION OF DEPOSITS IN COOLING SYSTEMS OF NUCLEAR REACTORS This invention relates to the ozone oxidation of deposits in cooling systems of nuclear reactors. The cooling systems of nuclear reactors tend to become coated with various radioactive deposits. While these deposits are not thick enough to plug the cooling systems, they do present a radiation hazard to personnel who must perform maintenance and repair work on them. Thus, it is necessary to remove the deposits in order to reduce the radioactivity to a level that is safe for personnel in the area. The deposits are conventionally removed by circulating through the cooling system a decontamination solution which solubilizes metal ions, and an oxidizing solution which oxidizes insoluble chromium oxides to the soluble dichromate ion. A typical decontamination solution consists of citric acid, oxalic acid, and a chelate, such as ethylenediaminetetraacetic acid (EDTA). A typical oxidizing solution consists of an alkali metal hydroxide and a permanganate. U.S. Patent Specification No. 4,287,002 discloses the decontamination of the cooling systems of nuclear reactors using ozone instead of alkali permanganate. A decontamination-oxidation-decontamination process is disclosed using ion exchange resins to remove ions from the solutions. Ozone offers several advantages over the alkali-permanganate in that it decomposes into oxygen and does not leave any ions remaining in the system, in addition to being an excellent oxidant. However, there are several disadvantages in using ozone as well, the principal one being its instability. This means that if the ozone must travel through a rather long cooling system, most of it will decompose before it reaches the end of the cooling system and the deposits in those portions of the cooling system will be insufficiently oxidized and will not be adequately removed. Accordingly, the present invention resides in a process for oxidizing chromium in deposits in the cooling system of a nuclear reactor using an aqueous solution of ozone, which comprises employing in said solution either (a) 0.01 to 0.5% of at least one water-soluble cerium IV compounds, (b) 0.01 to 0.5% of at least one water-soluble aromatic compound having at least one ketone group on an aromatic ring, or (c) mixtures of (a) and (b). Further according to the invention a composition comprises water, dissolved ozone, and either (a) 0.01 to 0.5% of a water-soluble cerium IV compound, (b) 0.01 to 0.5% of at least one water-soluble aromatic compound having at least one ketone group on an aromatic ring, or (c) mixtures of (a) and (b). The invention also includes a process for decontaminating the cooling system of a nuclear reactor which comprises the steps of shutting down said reactor, adding a decontamination composition to the coolant in said cooling system, circulating said coolant between a cation exchange resin and said cooling system until the radioactivity in said coolant leaving said cooling system is not substantially greater than the radioactivity of said coolant entering said cooling system, removing said decontamination composition from said coolant by passing said coolant through an anion exchange resin, adjusting the temperature of said coolant to from 40 to 100 C, adding compounds to said coolant so that said coolant comprises a composition according to that of the last preceding paragraph, circulating said coolant in said cooling system until the chromium concentration no longer increases substantially, raising the temperature of said coolant to at least 1000C, passing said coolant through an ion exchange resin containing an anion resin, adjusting the temperature of said coolant to from 60 to 2000C, and repeating the second, third, and fourth steps. We have thus discovered that the stability of an aqueous ozone oxidation solution for use in decontaminating the cooling systems of nuclear reactors can be greatly improved by the addition of a water-soluble cerium IV compound or a water-soluble aromatic compound having ketone groups on the aromatic ring, or both. Because the stability and solubility of the ozone are improved, the oxidizing power of the solution is not depleted in the remote reaches of the cooling system, and the oxidizing solution is more effective in removing the chromium from the deposits. This results in a high decontamination factor (i.e., the radioactivity before treatment divided by the radioactivity after treatment) during the subsequent decontamination solution treatment. This invention applies to the cooling system of any nuclear reactor, including pressurized water reactors, boiling water reactors, and high temperature gas nuclear reactors. The invention can be used on the deposits in the entire cooling system of a reactor using the aqueous coolant that is already present, or a special aqueous solution can be made up which is then circulated through any portion of the cooling system, such as the steam generator. The oxidizing solution used in this invention contains water, ozone, and either a water-soluble cerium IV compound or a water-soluble aromatic compound having ketone groups on the aromatic ring. Preferably, for maximum effectiveness, both the cerium IV compound and the aromatic compound are present. The ozone is dissolved in the water by sparging, which can produce a concentration of the ozone in the water from about 2x10 % (all percentages herein are by weight based on total solution weight) up to about saturation. No pH adjustment is necessary to the solution, but the pH will always be less than 7 because the components of the solution are acidic. The pH should not be permitted to rise to above 7 as that will result in the rapid decomposition of the ozone. The water-soluble cerium IV compound can be any compound that is water soluble and in which cerium is in the +4 oxidation state. Examples of suitable compounds includes ceric nitrate, ceric ammonium nitrate, ceric sulfate, ceric ammonium sulfate, and ceric sulfamate. The preferred compound is ceric ammonium nitrate because it is readily available, inexpensive, and very soluble in water. The cerium IV compound performs the function of oxidizing the chromium in the deposits in the cooling systems of the nuclear reactors, which reduces the cerium IV ion to a cerium III ion: llH20 + 6Ce+4 + Cr203 P 2H2CrO4 + 6Ce + 6H3 0+ Because the cerium IV compound is more stable than the ozone, it oxidizes the chromium farther away from the point of injection of the ozone into the cooling system, and is itself reduced to cerium III. When the cerium III compound returns to the point of injection of the ozone, the ozone oxidizes it back to cerium IV, thus regenerating it: 6H3 0+ + O3 + 6Ce+3 P 6Ce 4 + 9H20 From 0.01 to 0.5% of the water-soluble cerium IV compound can be used in the solution. If less is used, the solution will be less effective as there will be insufficient cerium IV compound to couple with the ozone, and more is unnecessary, wasted, and gives rise to large waste volumes. The preferred amount is from 0.08 to 0.12%. The water-soluble aromatic compound may be any aromatic compound that is water soluble and has at least one ketone group on an aromatic ring. Suitable aromatic compounds include naphthaquinone and quinone. Quinone is preferred as it readily forms an inclusion compound with ozone which increases the stability of the ozone and also increases it solubility. The amount of water-soluble aromatic compound in the solution can be from 0.01 and 0.5%. Less is ineffective and more is unnecessary and wasted. The preferred amount is from 0.05 to about 0.1. If the process of this invention is to be applied to the cooling system of a power reactor with the aqueous coolant in place, the reactor should first be shut down, which results in a lowering of the temperature of the coolant to from 60 to 2000C. In order to obtain the most effective decontamination of the cooling system, it is preferable to use a decontamination solution followed by an oxidizing solution followed by a decontamination solution. Thus, the first step in the process would be the addition of a decontamination composition to the coolant. Suitable decontamination compositions are well known in the art and typically consist of a mixture of organic acids, such as citric acid and oxalic acid, with organic chelates such as ethylene diaminetetraacetic acid. The coolant, containing the decontamination composition, is circulated between the cooling system where radioactive contaminating metal ions are dissolved and a cation exchange resin which removes the metal ions from the solution. The circulation is continued until the radioactivity in the coolant leaving the cooling system is not substantially greater than the radioactivity of the coolant entering the cooling system. The decontamination composition is then removed from the coolant by passing the coolant through an anion exchange resin. The temperature of the coolant is then lowered to from 40 to 1000C. Lower temperatures are difficult to achieve and higher temperatures will result in the decomposition of the ozone. The ozone, cerium IV compound, and/or the aromatic compound are then added to the coolant in amounts sufficient to give the concentrations specified. The coolant is then circulated until the chromium concentration in the coolant leaving the cooling system is not substantially greater than the chromium concentration in the coolant entering the cooling system. The temperature of the coolant is then raised to over 1000C in order to decompose the ozone. The coolant is passed through an ion exchange resin which contains an anion resin, such as an anion exchange resin or mixed anion/cation exchange resin, in order to remove the anions in the solution. The temperature of the coolant is then adjusted to from 60 to 2000C and the decontamination composition is again added and circulated through a cation exchange resin until the radioactivity level stabilizes. The decontamination composition is then removed from the coolant by passing the coolant through an anion exchange resin. This completes the decontamination of the cooling system. If a portion of the cooling system, such as the steam generator, is to be decontaminated, it is drained and the decontamination solution and oxidizing solutions are made up in tanks and are passed through that portion of the cooling system with water rinses in between. Otherwise, the procedure is identical.

Claims: CLAIMS: 1. A process for oxidizing chromium in deposits in the cooling system of a nuclear reactor using an aqueous solution of ozone, which comprises employing in said solution either (a) 0.01 to 0.5% of at least one watersoluble cerium IV compound, (b) 0.01 to 0.5% of at least one water-soluble aromatic compound having at least one ketone group on an aromatic ring, or (c) mixtures of (a) and (b). 2. A process according to claim 1, wherein the cerium IV compound is ceric ammonium nitrate. 3. A process according to claim 1 or 2, wherein the aromatic compound is quinone. 4. A process according to claim 1, 2 or 3, wherein the solution comprises the aqueous coolant of the nuclear reactor. 5. A process according to any of claims 1 to 4, wherein the solution containing (a), (b) or (c) is made up and passed through the cooling system. 6. A process according to any of claims 1 to 5, wherein the cooling system is in the steam generator of a pressurized water reactor. 7. A composition which comprises water, dissolved ozone, and either (a) 0.01 to 0.5% of a watersoluble cerium IV compound, (b) 0.01 to 0.5% of at least one water-soluble aromatic compound having at least one ketone group on an aromatic ring, or (c) mixtures of (a) and (b). 8. A composition according to claim 7, wherein the cerium IV compound is ceric ammonium nitrate. 9. A composition according to claim 8, wherein the aromatic compound is quinone. 10. A process for decontaminating the cooling system of a nuclear reactor which comprises the steps of shutting down said reactor, adding a decontamination composition to the coolant in said cooling system, circulating said coolant between a cation exchange resin and said cooling system until the radioactivity in said coolant leaving said cooling system is not substantially greater than the radioactivity of said coolant entering said cooling system, removing said decontamination composition from said coolant by passing said coolant through an anion exchange resin, adjusting the temperature of said coolant to from 40 to 1000C, adding compounds to said coolant so that said coolant comprises a composition according to claim 7, 8 or 9, circulating said coolant in said cooling system until the chromium concentration no longer increases substantially, raising the temperature of said coolant to at least 1000C, passing said coolant through an ion exchange resin containing an anion resin, adjusting the temperature of said coolant to from 60 to 2000C, and repeating the second, third and fourth steps. 11. A process according to claim 10, wherein the decontamination composition is an organic acid and a chelate.

Inventors: BECKER, LAWRENCE FREDERICK, JR., MURRAY, ALEXANDER PETER, SKRIBA, MICHAEL CHARLES, SLATER, CLIFTON GREENE
Applicants: WESTINGHOUSE ELECTRIC CORPORATION
Application year: 1984
Main classification: G21F9
IPC codes: G21C15, G21F9, G21D1