Electrochemical uranium nitride production

Patent metadata

Field	Value
Publication number	US-12018390-B2
Application number	US-202017753548-A
Country	US
Kind code	B2
Filing date	Sep 4, 2020
Priority date	Sep 10, 2019
Publication date	Jun 25, 2024
Grant date	Jun 25, 2024

Abstract

A method is described herein that produces UN from UF6 in at most two steps comprising UF6→intermediate→UN. The principle of the reaction is that in a first step, UF6 would be reduced to UxNy, where x may be an integer selected from 1 and 3, and y is an integer selected from 1 and 2. Reduction occurs at or near the surface of a gaseous membrane electrode where it is also in contact with a nitrogen bearing salt. In a second step, UxNy decomposes to UN and N2 gas, either in the same reactor as the first step or after removal to a separate unit for further processing.

First claim

What is claimed is:

1. A method for producing a uranium nitride fuel comprising:
a reaction represented by steps:
exposing UF 6 gas to a nitrogen bearing salt at or near a cathode to produce U x N y , where x is an integer of 1 or 2 and y is an integer of 1 to 3; and
converting U x N y to UN and nitrogen gas.

2. The method recited in claim 1 wherein the method is carried out in a batch process in a single reaction chamber.

3. The method recited in claim 1 wherein the method is carried out in a continuous process in a single reaction chamber.

4. The method recited in claim 1 wherein the method is carried out in a continuous process in two separate chambers.

5. The method recited in claim 1 wherein the nitrogen bearing salt is a nitride salt.

6. The method recited in claim 5 wherein the nitride salt is selected from the group consisting of alkali nitrides, alkaline nitrides, and transition metal nitrides.

7. The method recited in claim 5 wherein the method further comprises introducing nitrogen gas into the nitride salt.

8. The method recited in claim 5 wherein the nitrogen bearing salt is selected from the group consisting of NaCN, KCN, NaCNO, KCNO and mixtures thereof.

9. The method recited in claim 5 wherein the nitrogen bearing salt is selected from the group consisting of LiCl—KCl—Li 3 N, LiF—NaF—KF—Li 3 N and mixtures thereof.

10. The method recited in claim 1 wherein the nitrogen bearing salt is produce by introducing nitrogen gas into a neutral salt or a solvent.

11. The method recited in claim 1 wherein the nitrogen is N 15 .

12. The method recited in claim 1 further comprising reconstituting the nitrogen bearing salt by additions of nitrides to the salt.

13. The method recited in claim 1 wherein a voltage is applied to the cathode.

14. A method for producing a uranium nitride fuel comprising: a reaction represented by steps:
(1) xUF 6 +yN 3− →U x N y +6xF − and
(2) U x N y →xUN+(y−x)/2N 2 ;
wherein x is an integer of 1 or 2 and y is an integer of 1 to 3; and
the reaction being carried out on a porous UF6 membrane electrode of a first set of electrodes in contact with a nitrogen bearing salt.

15. The method recited in claim 14 wherein the nitrogen bearing salt is selected from the group consisting of alkali nitrides, alkaline nitrides, and transition metal nitrides.

16. The method recited in claim 14 wherein the nitrogen bearing salt includes one or both of UF 4 and UF 3 and step (2) takes place at an anode of a second set of electrodes in contact with the nitrogen bearing salt.

17. The method recited in claim 14 wherein the nitrogen bearing salt is selected from the group consisting of NaCN, KCN, NaCNO, KCNO and mixtures thereof.

18. The method recited in claim 14 wherein the nitrogen bearing salt is selected from the group consisting of LiCl—KCl—Li 3 N, LiF—NaF—KF—Li 3 N and mixtures thereof.

19. The method recited in claim 18 wherein step (1) of the reaction is represented by;
UF 6 +2Li 3 N→UN 2 +6LiF.

20. The method recited in claim 14 carried out at temperatures between 350 and 600° C.

21. The method recited in claim 14 further comprising:
reconstituting the reaction by nitride component additions.

22. The method recited in claim 14 further comprising:
reconstituting the reaction by replacing the porous UF 6 membrane electrode of the first set of electrodes or adding a second set of electrodes having a second porous UF 6 membrane electrode.

23. The method recited in claim 14 further comprising:
separating the U x N y from the salt by distilling the salt at a temperature sufficient for volatilizing the salt but maintaining the U x N y as a solid.

24. The method recited in claim 23 further comprising:
heating the solid U x N y to a temperature between 975° C. to less than 2500° C. to convert U x N y to UN.

25. The method recited in claim 23 further comprising:
condensing the distilled salt;
adding the condensed salt to the nitrogen bearing salt; and,
adding nitrides to the condensed salt.

26. The method recited in claim 23 wherein the temperature for volatilizing the salt is about 1200° C.

Assignees

• Westinghouse Electric Co Llc

Inventors

• Olson Luke C
• Metzger Kathryn E
• Lahoda Edward J

Classifications

• G21C21/02

  Manufacture of fuel elements or breeder elements contained in non-active casings · CPC title

• G21C3/62

  Ceramic fuel · CPC title

• C25B9/09

  Fused bath cells · CPC title

• C25B1/50

  Processes · CPC title

• C25B15/083

  Separating products · CPC title