Process For Dissolving Aluminum For Recovering Nuclear Fuel

Active Publication Date: 2016-12-01
THE UNITED STATES AS REPRESENTED BY THE DEPARTMENT OF ENERGY +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0008]In general, the present disclosure is directed to a process for controlling the dissolution of aluminum in an acid bath. More particularly, the process of the present disclosure is directed to dissolving aluminum under controlled conditions in order to positively affect off-gas production during the process. For instance, in one embodiment, the

Problems solved by technology

Fuel elements, including fuel rods in nuclear reactors, become unusable not so much on account of actual depletion of the fissionable fuel values, but because of the accumulation within the element of fission products.
These fission products can interfere with the neutron flux within the reactor.
Thus, the off-gas generation rate is never constant.
The mechanisms that imp

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Example

Example 1

[0035]Single-impurity scoping experiments to determine the influence of individual contaminants on off-gas rate were initially performed using Al-1100 alloy coupons. A series of four Al-1100 coupons were cut to the approximate dimensions of 19×11×3 mm. A 1 / 16 inch hole was drilled into each coupon in order to fasten each coupon to the glass rods used to lower them into a dissolving nitric acid solution. The coupons were lightly sanded, washed with soap and water, and then weighed and measured. Each coupon weighed approximately 1.7 g and had a surface area of approximately 6 cm2. Each coupon was tied by Teflon™ string through the 1116 inch hole to a glass rod on the dissolver apparatus that was labeled with the coupon position number for coupon identification.

[0036]A dissolver apparatus and off-gas collection system were assembled in a chemical hood. The dissolver apparatus contained a boiling flask with multiple ports, a condenser, an in-line gas sample glass bulb, and a wat

Example

[0037]Experiment 1 was conducted using a dissolving solution of 7 M HNO3, 0.1 M KF, and 0.002 M Hg, and no contaminants. Nominally 150 mL of dissolving solution was weighed, added to a flask containing a Teflon™ stir bar, and then sealed. The dissolution vessel and off-gas collection system (including 8 sample glass bulbs) were leak checked by filling the system with Ar to inflate the Tedlar™ bag and observing a constant water column height over several minutes. The stir bar rotation was set at 325 rpm. The dissolving solution was then heated to 100° C. The off-gas system was vented to relieve pressure (to zero the off-gas collection system), and a stopwatch was started as the first of four Al-1100 coupons was lowered into the solution.

[0038]To measure the gas generation rate, time versus water displacement was manually recorded until the coupon was visually observed to have dissolved completely. For each coupon dissolution, a gas sample was taken generally at 450 mL of off-gas volume

Example

Example 2

[0041]Another series of experiments were performed to determine the impact of Fe on off-gas generation rates for uranium-aluminum dissolution at higher concentrations of Hg. A series of four 30 wt % U—Al alloy coupons, cut to 20×12×3 mm with a mass of 1.6-2.1 g, were prepared as described in Example 1.

[0042]Experiment 3 was conducted using a method analogous to that of Example 1 with a dissolving solution of 7 M HNO3, 0.1 M KF, 0.012 M Hg, and no Fe contamination. Hg was initially present in the solution, and the solution was heated to 100° C. before lowering the first coupon. The concentration of hydrogen in the off-gas was measured using gas chromatography.

[0043]Experiment 4 was conducted using a dissolving solution of 7 M HNO3, 0.1 M KF, 0.012 M Hg, and no Fe contamination. Approximately 130 mL of dissolving solution was weighed and added to the dissolver flask containing a Teflon™ stir bar. The solution containing all components except Hg was then heated to 100° C. A syrin

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Abstract

A process for controlling the dissolution of a metal in an acid bath is described. The metal may comprise aluminum and the acid bath may contain a metal catalyst that causes the metal to dissolve. In order to control the rate of dissolution and/or the amount of gas evolved during the process, an iron source is added to the bath. In one embodiment, the process can be used to dissolve aluminum contained in spent fuel assemblies for recovering a nuclear fuel, such as uranium.

Description

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Claims

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Application Information

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Owner THE UNITED STATES AS REPRESENTED BY THE DEPARTMENT OF ENERGY
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