Patent Number: 047643382
Section: claims

1. In the method of controlling the dissolution of radioactive corrosion products deposited on the surface of fuel rods into the core water of a boiling water-type atomic power plant including a nuclear reactor having a recycling system with a reactor water-purifying unit, a turbine generator driven by steam generated in the nuclear reactor, a condensor, a condensed water-purifying unit, and a water heater positioned in the recycling system; wherein the improvement comprises, passing the reactor water of the recycling system through the reactor water-purifying unit containing a cation exchange resin, wherein a portion of said cation exchange resin had been previously replaced with an alkali metal-form cation exchange resin, and passing the condensed water of the recycling system through a condensed water-purifying unit containing a cation exchange resin, wherein a portion of said cation exchange resin had been previously replaced with an alkali metal-form cation exchange resin, so as to cause the pH of the reactor water and condensed water to be adjusted to a pH of between about 7.0 and 8.5 through the ion exchange reaction of the alkali metal-form cation exchange resins with the cations contained in the reactor water and the condensor water of the recycling system whereby the dissolution of radioactive corrosion products deposited on the surface of the fuel rods into the core water of a boiling water-type atomic power plant is controlled. 2. The method of claim 1 wherein said pH is maintained between 7.5 and 8.0. 3. The method of claim 1 wherein said radioactive corrosion product is cobalt ferrite. 4. The method of claim 1 wherein said radioactive corrosion product is nickel ferrite. 5. The method of claim 1 wherein said alkali-form cation exchange resins is a Na-form cation exchange resin. 6. The method of claim 1 wherein the reactor water-purifying unit and the condensed water-purifying unit contain a mixture of cation exchange resin and anion exchange resin with said cation exchange resin being in excess of said anion exchange resin, wherein said excess portion of the cation exchange resin is regenerated together with the anion exchange resin with an alkali, thereby converting the excess portion of the cation exchange resin into an alkali-form cation exchange resin. 7. The method of claim 6 wherein said alkali-form cation exchange resin is a Na-form cation exchange resin. 8. The method according to claim 7 wherein the ratio of the Na-form cation exchange resin produced to the total cation exchange resin is 0.1 to 0.5. 9. The method of claim 7 wherein said Na-form cation exchange resin has the formula R--(SO.sub.3 Na).sub.2.