IP Library › Granted Patent US 12,431,253
Granted Patent B2
US 12,431,253 · App. 18/663,976 · Granted Sep 30, 2025

Fission product extraction system and methods of use thereof

Inventors: Kim Pamplin (Abilene, TX); Diego Zometa (Abilene, TX)
Assignee: Abilene Christian University
G21C19/307G21G1/001G21C19/30G21G2001/0036
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Quick Facts
Patent No.
US 12,431,253
App. No.
18/663,976
Granted
Sep 30, 2025
Kind
B2
Abstract

A molten salt reactor system may produce fission products, such as molybdenum-99, which may be extracted by an extraction system. The extraction system may be configured to sparge the molten fuel salt with an inert gas to dislodge gaseous fission products from the molten fuel salt, so that the gaseous fission products flow through an off-gas outlet into a gas transfer assembly. The example extraction system may also include introducing a gaseous halogenating agent to prevent the fission products from depositing on a pipe surface of the gas transfer assembly. The gaseous fission products may flow from the gas transfer assembly to a carboy containing an aqueous solution, to process and/or filter the fission products. The resulting solution containing processed fission products in the carboy may be further distilled into final, usable products.

Claims (77)

1. A fission product extraction system comprising:

a vessel fluidly connected to a molten salt loop of a molten salt reactor system, wherein the vessel is configured to receive a flow of fueled molten salt comprising dissolved fission products from the molten salt loop; and

an extraction assembly fluidly coupled to the vessel and comprising

a first gas conduit configured to introduce inert gas into the vessel and dislodge the dissolved fission products from the fueled molten salt;

a gas transfer assembly configured to receive the dislodged fission products from the vessel,

a second gas conduit fluidly connected to the gas transfer assembly, and configured to feed a gas into the gas transfer assembly and move the dislodged fission products therethrough, and

a carboy fluidly connected to the gas transfer assembly and configured to receive the dislodged fission products and dissolve the dislodged fission products into a liquid solution contained within the carboy; and

wherein the fission products are dislodged from the fueled molten salt in a gaseous phase by diffusion through agitation caused by the inert gas contacting the fueled molten salt, wherein the gas transfer assembly includes a gas outlet positioned on a top side of the vessel, and wherein the gaseous phase fission products ascend into the gas outlet upon dislodgment.

2. The fission product extraction system of claim 1 , further comprising a purification system comprising

an extraction cartridge configured to receive the liquid solution containing the dissolved fission products from the carboy, wherein the extraction cartridge is operable to absorb fission products from the liquid solution;

wherein fission products are retained in a sorbent of the extraction cartridge as the dissolved fission products in the liquid solution from the carboy are passed through the extraction cartridge; and

wherein the retained fission products are eluted from the sorbent into a generator configured to store the fission products.

3. The fission product extraction system of claim 2 , wherein the extraction cartridge is operable to selectively isolate fission products from one another by configuring the sorbent to absorb the selected fission products and elute other fission products of the fission products.

4. The fission product extraction system of claim 2 , wherein the extraction cartridge and/or the carboy are removable while containing the dislodged fission products from the fission product extraction system for offsite processing.

5. The fission product extraction system of claim 3 , wherein the extraction cartridge is configured to be fluidly connected to the generator and a waste container, wherein the extraction system includes piping and at least one valve to selectively direct fission products from the extraction cartridge to the generator or the waste container.

6. The fission product extraction system of claim 1 , wherein the first gas conduit includes a porous tube extending into an internal volume of the vessel and configured to feed the inert gas into the vessel through a plurality of pores of the porous tube.

7. The fission product extraction system of claim 1 , wherein the first gas conduit is configured to feed the inert gas about an internal periphery of the vessel.

8. The fission product extraction system of claim 7 , wherein the first gas conduit includes a porous toroidal tube positioned at a lower section of the vessel and configured to feed the inert gas into the vessel through a plurality of pores of the porous toroidal tube.

9. The fission product extraction system of claim 1 , wherein the first gas conduit includes a support rod vertically extending from a bottom side of the vessel into an internal volume of the vessel, wherein the support rod includes at least one horizontally extending porous blade configured to feed the inert gas into the vessel through a plurality of pores of the at least one porous blade as the at least one porous blade spins about the support rod.

10. The fission product extraction system of claim 2 , wherein the extraction cartridge is a Solid Phase Extraction (SPE) cartridge including at least one alumina sorbent.

11. The fission product extraction system of claim 1 , wherein the second gas conduit is configured to feed the gas throughout piping of the gas transfer assembly and wherein the second gas conduit is configured to feed the gas in the direction of the carboy to facilitate receipt of the dislodged fission products by the carboy.

12. The fission product extraction system of claim 1 , wherein the gas includes a halogenating agent operable to react with precipitated fission products deposited on piping of the transfer assembly.

13. The fission product extraction system of claim 1 , wherein the gas transfer assembly includes at least one heat wrap configured to heat a surface of piping of the gas transfer assembly.

14. The fission product extraction system of claim 1 , wherein the dissolved fission products comprise molybdenum.

15. The fission product extraction system of claim 1 , wherein the inert gas comprises helium gas.

16. The fission product extraction system of claim 12 , wherein the halogenating agent comprises nitrogen trifluoride.

17. A system comprising:

a fuel salt system configured to circulate an irradiated fueled molten salt comprising dissolved fission products through a molten salt loop of a molten salt reactor system including an access vessel, a reactor, a heat exchanger; and

an extraction system fluidly coupled to the access vessel along the molten salt loop and comprising

the access vessel fluidly connected to the molten salt loop of the molten salt reactor system and configured receive a flow of irradiated fueled molten salt from the reactor of molten salt reactor system following nuclear fission;

a first gas conduit fluidly connected to the access vessel and configured to sparge and dislodge the dissolved fission products from the irradiated fueled molten salt; and

a gas transfer assembly fluidly connected to the access vessel and configured to receive the dislodged fission products and direct the sparged fission products to a carboy;

a second gas conduit fluidically connected to the gas transfer assembly, and configured to feed a gas into the gas transfer assembly and move the dislodged fission products therethrough;

wherein the carboy is fluidly connected to the gas transfer assembly and configured to receive the sparged fission products and dissolve the sparged fission products into a liquid solution contained within the carboy; and

wherein the fission products are dislodged from the irradiated fueled molten salt in a gaseous phase by diffusion through agitation caused by an inert gas contacting the irradiated fueled molten salt, wherein the gas transfer assembly includes a gas outlet positioned on a top side of the access vessel, and wherein the gaseous phase fission products ascend into the gas outlet upon dislodgment.

18. The system of claim 17 , further comprising a purification system comprising

a Solid Phase Extraction (SPE) cartridge configured to receive the dissolved fission products from the carboy;

wherein the SPE cartridge is operable to absorb fission products from the liquid solution;

wherein fission products are retained in a sorbent of the SPE cartridge as the dissolved fission products in the liquid solution from the carboy are passed through the SPE cartridge;

wherein the retained fission produces are eluted from the sorbent into a generator configured to store the concentrated fission products.

19. The system of claim 18 , wherein the SPE cartridge receives the dissolved fission products from the carboy by a continuous flow or by batch.

20. The system of claim 1 , further comprising a reactor pump fluidly coupled to the vessel operable to facilitate circulation of the fueled molten salt to the vessel.

21. The system of claim 20 , further comprising a heat exchanger connected to the molten salt loop and positioned downstream of the reactor pump and the vessel, such that the heat exchanger receives the fueled molten salt following extraction of the dissolved fission products.

22. A method for extracting fission products from irradiated fueled molten salt of a molten salt reactor system comprising:

sparging a reactor access vessel that is fluidly connected to a molten salt loop of the molten salt reactor system with an inert gas by an extraction assembly fluidly coupled to the reactor access vessel;

wherein the reactor access vessel is configured to receive a flow of fueled molten salt comprising dissolved fission products from the molten salt loop;

wherein the extraction assembly comprises a first gas conduit configured to introduce the inert gas into the reactor access vessel;

dislodging dissolved fission products from the irradiated fueled molten salt via the introduction of the inert gas into the reactor access vessel by the first gas conduit by agitation of the irradiated fueled molten salt by the inert gas;

receiving the dislodged fission products from the irradiated fueled molten salt by a gas transfer assembly of the extraction assembly fluidly connected to the reactor access vessel;

feeding a gas into the gas transfer assembly as the gas transfer assembly receives the dislodged fission products; and

wherein the extraction assembly further comprises a second gas conduit fluidly connected to the gas transfer assembly, and configured to feed the gas into the gas transfer assembly and move the dislodged fission products therethrough;

dissolving the dislodged fission products into a liquid solution in a carboy of the extraction assembly fluidly connected to the gas transfer assembly and configured to receive the dislodged fission products; and

wherein the dissolved fission products are dislodged from the irradiated fueled molten salt in a gaseous phase by diffusion through agitation caused by the inert gas contacting the irradiated fueled molten salt, wherein the gas transfer assembly includes a gas outlet positioned on a top side of the reactor access vessel, and wherein the gaseous phase fission products ascent into the gas outlet upon dislodgement.

23. The method of claim 22 , further comprising:

purifying the dissolved fission products by providing an extraction cartridge configured to receive and absorb the dissolved fission products from the liquid solution of the carboy;

isolating selected fission products by washing a sorbent of the extraction cartridge;

eluting the selected fission products from the sorbent into a generator.

24. The method of claim 23 , further comprising concentrating the selected fission products by continually passing the liquid solution of the carboy through the extraction cartridge.

25. The method of claim 22 , wherein the fission products comprise molybdenum.

26. The method of claim 22 , further comprising circulating the irradiated fueled molten salt through a reactor of the molten salt reactor system causing fission reactions.

27. The method of claim 22 , further comprising circulating the irradiated fueled molten salt through a heat exchanger following removal of the dissolved fission products.

28. The method of claim 22 , wherein the inert gas comprises helium gas and wherein the gas comprises nitrogen trifluoride.

29. A fission product extraction system comprising:

a vessel fluidly connected to a molten salt loop of a molten salt reactor system, wherein the vessel is configured to receive a flow of fueled molten salt comprising dissolved fission products from the molten salt loop;

an extraction assembly fluidly coupled to the vessel and comprising

a first gas conduit configured to introduce inert gas into the vessel and dislodge the dissolved fission products from the fueled molten salt;

a gas transfer assembly configured to receive the dislodged fission products from the vessel,

a second gas conduit fluidly connected to the gas transfer assembly, and configured to feed a gas into the gas transfer assembly and move the dislodged fission products therethrough, and

a carboy fluidly connected to the gas transfer assembly and configured to receive the dislodged fission products and dissolve the dislodged fission products into a liquid solution contained within the carboy; and

a purification system comprising

an extraction cartridge configured to receive the liquid solution containing the dissolved fission products from the carboy, wherein the extraction cartridge is operable to absorb fission products from the liquid solution;

wherein fission products are retained in a sorbent of the extraction cartridge as the dissolved fission products in the liquid solution from the carboy are passed through the extraction cartridge; and

wherein the retained fission products are eluted from the sorbent into a generator configured to store the fission products.

30. The fission product extraction system of claim 29 , wherein the extraction cartridge is operable to selectively isolate fission products from one another by configuring the sorbent to absorb the selected fission products and elute other fission products of the fission products.

31. The fission product extraction system of claim 29 , wherein the extraction cartridge and/or the carboy are removable while containing the dislodged fission products from the fission product extraction system for offsite processing.

32. The fission product extraction system of claim 30 , wherein the extraction cartridge is configured to be fluidly connected to the generator and a waste container, wherein the extraction system includes piping and at least one valve to selectively direct fission products from the extraction cartridge to the generator or the waste container.

33. The fission product extraction system of claim 29 , wherein the extraction cartridge is a Solid Phase Extraction (SPE) cartridge including at least one alumina sorbent.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 14, 2024
From: PAMPLIN, KIM; ZOMETA, DIEGO
To: ABILENE CHRISTIAN UNIVERSITY
Reel/Frame 067410/0822 →
Continuity (2)
Provisional Application 63509491 · Jun 21, 2023
Related Publication 20240428961A1 · Dec 26, 2024
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