IP Library › Granted Patent US 9,761,338
Granted Patent B2
US 9,761,338 · App. 14/288,045 · Granted Sep 12, 2017

Method and apparatus for preparing spent nuclear fuel for dry storage

Inventor: Krishna P. Singh (Hobe Sound, FL)
G21F5/005F26B21/006F26B21/08F26B21/14G21C19/32G21F9/28F26B5/04G21F5/008
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Quick Facts
Patent No.
US 9,761,338
App. No.
14/288,045
Granted
Sep 12, 2017
Kind
B2
Abstract

A system and method for drying cavities containing spent nuclear fuel is devised. The invention utilizes a non-intrusive procedure that is based on monitoring the dew point temperature of a non-reactive gas that is circulated through the cavity. In one aspect, the invention is a system for drying a cavity loaded with spent nuclear fuel comprising: a canister forming the cavity, the cavity having an 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; and means for repetitively measuring the dew point temperature of the non-reactive gas exiting the cavity.

Claims (20)

1. A method of preparing spent nuclear fuel for dry storage drying comprising:

a) flowing a non-reactive gas through a cavity containing spent nuclear fuel;

b) repetitively measuring dew point temperature of the non-reactive gas exiting the cavity;

(c) drying the non-reactive gas that exits the cavity after the dew point temperature is measured;

(d) subsequent to step (c), re-circulating the dried non-reactive gas through the cavity in a closed flow loop; and

(e) subsequent to step (d), upon the dew point temperature of the nonreactive gas exiting the cavity being measured to be at or below a predetermined dew point temperature for a predetermined period of 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 containing the spent nuclear fuel 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 wherein step d) comprises drying the non-reactive gas with a desiccant.

8. The method of claim 1 wherein step d) comprises drying the non-reactive gas by chilling the non-reactive gas.

9. 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.

10. 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.

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;

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 the canister is positioned in a cask.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 12, 2014
From: SINGH, KRISHNA P.
To: HOLTEC INTERNATIONAL,INC.
Reel/Frame 033731/0735 →
Continuity (4)
Continuation 13622343 · Sep 18, 2012
Continuation 12641378 · Dec 18, 2009
Division 11145785 · Jun 6, 2005
Related Publication 20140317952A1 · Oct 30, 2014