Patent Number: 
Section: claims

1. A method of preparing spent nuclear fuel for dry storage comprising:a) flowing a non-reactive gas through a cavity;b) repetitively measuring dew point temperature of the non-reactive gas exiting the cavity; andc) upon the dew point temperature of the non-reactive gas exiting, the cavity being measured to be at or below a predetermined dew point temperature for a predetermined time, discontinuing the flow of the non-reactive gas and sealing the cavity. 2. The method of claim 1 wherein step (a) comprises flowing the non-reactive gas through the cavity at a predetermined flow rate. 3. The method of claim 2 wherein the cavity has a volume and the predetermined flow rate is chosen so that the volume of the cavity is turned over 25 to 50 times per hour. 4. The method of claim 1 wherein the predetermined dew point temperature is selected to correspond to a desired vapor pressure within the cavity. 5. The method of claim 1 wherein the predetermined dew point temperature is in a range of approximately 20 to 26° F., and the predetermined time is in a range of approximately 25 to 35 minutes. 6. The method of claim 5 wherein the predetermined dew point temperature is approximately 22.9° F. and the predetermined time is approximately 30 minutes. 7. The method of claim 1 further comprising:d) drying the on-reactive gas that exits the cavity after the dew point temperature is measured; ande) re-circulating the dried non-reactive gas through the cavity. 8. The method of claim 7 wherein step d) comprises drying the non-reactive gas with a desiccant. 9. The method of claim 7 wherein step d) comprises drying the non-reactive gas by chilling the non-reactive gas. 10. The method of claim 1 wherein the non-reactive gas is nitrogen, carbon dioxide, light hydrocarbon gases, or a noble gas selected from the group consisting of helium, argon, neon, radon, krypton, and xenon. 11. The method of claim 1 wherein the predetermined dew-point temperature is selected to correspond to a vapor pressure of 3 Torr or less in the cavity. 12. The method of claim 1 further comprising:d) drying the non-reactive gas that exits the cavity after the dew point temperature is measured;e) re-circulating the dried non-reactive gas through the cavity;wherein the predetermined dew-point temperature is selected to correspond to a vapor pressure of 3 Torr or less in the cavity;wherein step (a) comprises flowing the non-reactive gas through the cavity at a predetermined flow rate that results in a volume of the cavity being turned over 25 to 50 times per hour;wherein the non-reactive gas is helium;wherein the cavity is formed by a canister and is loaded, with spent nuclear fuel, the canister positioned in a cask. 13. A system for drying a cavity loaded with spent nuclear fuel comprising a canister forming the cavity, the cavity havingan inlet and an outlet;a source of non-reactive gas;means for flowing the non-reactive gas from the source of non-reactive gas through the cavity; andmeans for repetitively measuring the dew point temperature of the non-reactive gas exiting the cavity. 14. The system of claim 13 further comprising means for drying the non reactive gas, the drying means located downstream of the of the dew point temperature measuring means. 15. The system of claim 14 wherein the drying means comprises a chiller. 16. The system of claim 14 wherein the drying means comprises a desiccant. 17. The system of claim 14 further comprising means for re-circulating the non-reactive gas from the drying means back into the non-reactive gas source. 18. The system of claim 13 further comprising:a controller operably coupled to the dew point temperature measuring, means;wherein the dew point temperature measuring means is adapted to create signals indicative of the measured dew point temperature of the non-reactive gas and transmit the signals to the controller; andwherein the controller is adapted to analyze the signals and upon determining that the signals indicate that the measured dew point temperature is at or below a predetermined dew point temperature for a predetermined time the controller is further adapted to (1) cease flow of the non-reactive gas through the cavity; and/or (2) activate a means for indicating that the cavity is dry. 19. The system of claim 13 further comprising a cask, the canister positioned within the cask. 20. The system of claim 13 further comprising:a cask, the canister positioned within the cask;means for drying the non-reactive gas, the drying means located downstream of the dew point temperature measuring means;means for re-circulating the non-reactive gas from the drying means back into the non-reactive gas source, thereby forming a closed-loop system;a controller operably coupled to the dew point temperature measuring means;wherein the dew point temperature measuring means is adapted to create signals indicative of the measured dew point temperature of the non-reactive gas and transmit the signals to the controller; andwherein the controller is adapted to analyze the signals and upon determining that the signals correspond to the measured dew point temperature being at or below a predetermined dew point temperature for a predetermined time, the controller is further adapted to (1) cease flow of the non-reactive gas through the cavity; and/or (2) activate a means for indicating that the cavity is dry;wherein the predetermined dew point temperature is in a range of approximately 20 to 26° F., the predetermined time is in a range of approximately 25 to 35 minutes, and the flowing means circulates the non-reactive gas through the cavity at a predetermined flow rate that results in a volume of the cavity being turned over 25 to 50 times per wherein the dew point temperature measuring means comprises a hygrometer.