Electrochemical ion separation in molten salts
A purification method that uses ion-selective ceramics to electrochemically filter waste products from a molten salt. The electrochemical method uses ion-conducting ceramics that are selective for the molten salt cations desired in the final purified melt, and selective against any contaminant ions. The method can be integrated into a slightly modified version of the electrochemical framework currently used in pyroprocessing of nuclear wastes.
1. A method for separating contaminants from a molten salt, comprising:
providing an electrochemical cell, the electrochemical cell comprising:
an ion-selective ceramic membrane having selectivity for at least one molten salt cation and selectivity against transport of at least one contaminant cation,
a purified molten salt electrolyte on a cathode side of the ceramic membrane and a contaminated molten salt electrolyte on an anode side of the ceramic membrane,
a cathode immersed in a purified molten salt electrolyte on the cathode side of the ceramic membrane, and
an anode immersed in a contaminated molten salt electrolyte comprising the at least one molten salt cation and the at least one contaminant cation on the anode side of the ceramic membrane; and
applying an electrical bias across the anode and the cathode, thereby causing the at least one molten salt cation to transport across the ceramic membrane but substantially excluding the at least one contaminant cation from transporting across the ceramic membrane and thereby concentrating the at least one contaminant ion in the contaminated molten salt electrolyte on the anode side of the ceramic membrane.
2. The method of claim 1 , wherein the ion-selective ceramic membrane is selective by size exclusion or valence-charge exclusion of the at least one contaminant cation.
3. The method of claim 1 , wherein the ion-selective ceramic membrane comprises Na 1+x Zr 2 Si x P 3-x O 12 .
4. The method of claim 3 , wherein the Na 1+x Zr 2 Si x P 3-x O 12 comprises cation-substituted Na 1+x Zr 2 Si x P 3-x O 12 .
5. The method of claim 4 , wherein the cation-substituted Na 1-x Zr 2 Si x P 3-x O 12 comprises KZr 2 (PO 4 ) 3 .
6. The method of claim 1 , wherein the ion-selective ceramic membrane comprises a garnet-structured lithium lanthanum tantalate ceramic.
7. The method of claim 6 , wherein the garnet-structured lithium lanthanum tantalate ceramic comprises Li 6 BaLa 2 Ta 2 O 12 .
8. The method of claim 1 , wherein the purified and contaminated molten salt electrolytes comprise LiCl—KCl.
9. The method of claim 8 , wherein the purified and contaminated molten salt electrolytes comprise a eutectic of LiCl—KCl.
10. The method of claim 8 , wherein chloride ions in the contaminated molten salt electrolyte are oxidized to form chlorine gas at the anode and the chlorine gas is reduced to chloride ions at the cathode.
11. The method of claim 1 , wherein the at least one contaminant cation comprises a fission product.
12. The method of claim 1 , wherein the at least one contaminant cation comprises a monovalent cation.
13. The method of claim 12 , wherein the monovalent cation comprises Cs + .
14. The method of claim 1 , wherein the at least one contaminant cation comprises a divalent cation.
15. The method of claim 14 , wherein the divalent cation comprises Cu 2+ or Sr 2+ .
16. The method of claim 1 , wherein the anode comprises copper.
17. The method of claim 1 , wherein the cathode comprises platinum, carbon, tungsten, copper, or steel.
18. The method of claim 1 , wherein the ion-selective ceramic membrane comprises a planar configuration.
19. The method of claim 1 , wherein the ion-selective ceramic membrane comprises a tubular configuration.