Direct electrochemical reduction of metal-oxides

• US 6,540,902 B1
• Filed: 09/05/2001
• Issued: 04/01/2003
• Est. Priority Date: 09/05/2001
• Status: Expired due to Fees

• Current Assignee: US Department of Energy (Government of the United States of America)
• Original Assignee: United States Department of Energy (Government of the United States of America)
• Inventors: Gourishankar, Karthick, Redey, Laszlo I.
• Primary Examiner(s): Nguyen, Nam
• Assistant Examiner(s): Parsons, Thomas H.
• Application Number:
  US09/945,721
• Time in Patent Office: 573 Days
• Field of Search: 205/47, 205/336, 205/354, 205/367-372, 205/397, 205/406
• US Class Current: 205/354
• CPC Class Codes: C25C 3/00 Electrolytic production, recovery or refining of metals by electrolysis of melts C25C5/00 takes precedence
• CPC Class Codes: C25C 3/34 of metals not provided for in groups C25C3/02 - C25C3/32
• CPC Class Codes: C25C 7/005 of cells for the electrolysis of melts C25C7/02 - C25C7/06 take precedence

Abstract

A method of controlling the direct electrolytic reduction of a metal oxide or mixtures of metal oxides to the corresponding metal or metals. A non-consumable anode and a cathode and a salt electrolyte with a first reference electrode near the non-consumable anode and a second reference electrode near the cathode are used. Oxygen gas is produced and removed from the cell. The anode potential is compared to the first reference electrode to prevent anode dissolution and gas evolution other than oxygen, and the cathode potential is compared to the second reference electrode to prevent production of reductant metal from ions in the electrolyte.

Claims

1. A method of controlling the direct electrolytic reduction of a metal oxide or

mixtures of metal oxides to the corresponding metal or metals comprising establishing a non-consumable anode and a cathode in contact with a molten salt electrolyte having mobile oxygen ions and reductant metal ions, providing a first reference electrode near the non-consumable anode and a second reference electrode near the cathode, establishing a substantially constant voltage across the anode and cathode or passing a substantially constant current between the anode and the cathode to reduce the metal oxide or oxide mixtures to the corresponding metal or metals while producing oxygen gas, and monitoring the anode potential compared to the first reference electrode to prevent anode dissolution and gas evolution other than oxygen, and monitoring the cathode potential compared to the second reference electrode to prevent production of reductant metal from ions in the electrolyte.

2. The method of claim 1, wherein the anode is selected from the group consisting of Pt, SnO₂, LiFeO₂ and Li_xFe_yNi₍₁₋

y)O_z.

3. The method of claim 1, wherein the reference electrode is selected from the group consisting of Li/Li₂O, Ni/NiO, and Fe/Fe₃O₄.

4. The method of claim 1, wherein the cathode consists of two components.

5. The method of claim 4, wherein the cathode includes a current lead of stainless steel or Ta and a bed of the metal oxide to be reduced in a container of stainless steel or Ta or a porous ceramic.

6. The method of claim 1, wherein the anode includes an oxygen venting system.

7. The method of claim 6, wherein the oxygen venting system includes a ceramic shroud for collecting oxygen produced at the anode.

8. The method of claim 7, wherein the oxygen collected in the shroud is removed from the anode.

9. The method of claim 1, wherein reduction is of a metal oxide or metal oxide mixtures with a lithium chloride containing electrolyte maintained at a temperature of from about 400°

C. to about 700°

C. having Li₂O dissolved therein.

10. The method of claim 1, wherein reduction is of a rare earth oxide or oxides with a calcium chloride containing electrolyte maintained at a temperature of about 600°

C.-1100°

C. and having CaO dissolved therein.

11. The method of claim 1, wherein a mobile oxygen ion concentration is maintained substantially constant in the electrolyte during the reduction of the metal oxide.

12. The method of claim 11, wherein the metal is U or alloys thereof.

13. The method of claim 11, wherein the metal is Nd or its alloys.

14. The method of claim 11, wherein the metal oxide is an actinide oxide.

15. The method of claim 11, wherein the metal oxide is a rare earth oxide.

16. The method of claim 11, wherein the metal oxide is one or more of Ca oxide, lithium oxide, vanadium oxide, titanium oxide, tantalum oxide and tungsten oxide.

17. The method of claim 1, wherein the metal oxide is substantially insoluble in the molten salt electrolyte.

18. The method of claim 1, wherein the electrolyte is one or more of LiCl₂, CaCl₂, LiCl—

CaCl₂, LiCl—

KCl and the alkali or alkaline earth metal fluorides.

19. The method of claim 1, wherein a cathode assembly includes a basket of predetermined size and shape.

20. The method of claim 1, wherein the total quantity of oxygen evolved is determined and used to calculate the extent of metal oxide reduction.

21. The method of claim 1, wherein the cathode is vibrated during reduction.

22. The method of claim 1, wherein the electrolyte is agitated during reduction.

23. A method of electrochemically reducing metal oxide comprising establishing a molten chloride or fluoride electrolyte having mobile oxide ions and reductant metal ions therein under an inert atmosphere, positioning an oxygen stable anode assembly surrounded by a shroud of substantially oxygen impervious material and a first reference electrode in the molten electrolyte, positioning a cathode assembly including a porous container for the metal oxide and a second reference electrode in the molten electrolyte, establishing a substantially constant potential across the anode assembly and the cathode assembly or passing a substantially constant current between the anode assembly and the cathode assembly to reduce metal oxide or oxide to metal or metals at the cathode while producing oxygen gas at the anode, periodically interrupting the electrolytic process to determine the anode potential relaxation with respect to the first reference electrode and to determine the cathode potential relaxation with respect to the second electrode and adjusting the potential across the anode assembly and the cathode assembly or the current to prevent anode dissolution or production of reductant metal from its ions in the electrolyte and to maintain the reductant metal production such that the reductant metal is being consumed in a chemical reaction with the oxide to be reduced at about the same overall rate as the reductant metal is being produced.

24. The method of claim 23, wherein a chlorine stable anode assembly is substituted for the oxygen stable anode assembly when the concentration of oxide ions is reduced toward zero.

25. The method of claim 23, wherein a shroud extends out of the electrolyte to contain oxygen gas produced at the anode and prevents oxygen from recombining with the metal produced at the cathode, and prevents corrosion of cell components, and prevents contamination of the inert gas atmosphere of the cell components.

26. The method of claim 25, wherein the shroud is high density MgO or Al₂O₃.

27. The method of claim 23, wherein two or more anode assemblies are operated in conjunction with one or more cathode assemblies.