Methods of recovering a metal from a metal-containing waste material and related electrochemical cells

Patent metadata

Field	Value
Publication number	US-2023046888-A1
Application number	US-202217819239-A
Country	US
Kind code	A1
Filing date	Aug 11, 2022
Priority date	Aug 11, 2021
Publication date	Feb 16, 2023
Grant date	—

Abstract

A method of recovering a metal from a metal-containing waste material comprises heating a metal-containing waste material under a hydrogen flow to form a hydrided metal material. Hydrogen is removed from the hydrided metal material to form an elemental metal or a metal oxide. Additional methods are disclosed, as are related electrochemical cells.

First claim

What is claimed is:

1 . A method of recovering a metal from a metal-containing waste material, comprising:
heating a metal-containing waste material under a hydrogen flow to form a hydrided metal material; and removing hydrogen from the hydrided metal material to form an elemental metal or a metal oxide.

2 . The method of claim 1 , wherein heating a metal-containing waste material under a hydrogen flow to form a hydrided metal material comprises selectively hydriding one or more metals including metal compounds and metal oxides of the metal-containing waste material.

3 . The method of claim 1 , wherein heating a metal-containing waste material under a hydrogen flow to form a hydrided metal material comprises forming neodymium hydride, platinum hydride, or titanium hydride.

4 . The method of claim 1 , wherein removing hydrogen from the hydrided metal material to form an elemental metal or a metal oxide comprises removing the hydrogen in an electrochemical cell.

5 . The method of claim 1 , further comprising separating one or more metals of the metal-containing waste material from other metals of the metal-containing waste material using a molten salt electrochemical process to obtain a metal material, a physical separation, and combinations thereof.

6 . The method of claim 5 , further comprising annealing the metal material under reducing conditions.

7 . The method of claim 1 , wherein the hydrogen flow is maintained at a positive pressure under conditions that make up hydrogen as the hydrided metal material is formed.

8 . The method of claim 1 , further comprising separating the hydrided metal material from unhydrided metal material; and
wherein removing hydrogen from the hydrided metal material is done in a pyrovacuum stage.

9 . The method of claim 1 , further comprising separating the hydrided metal material from unhydrided metal material, comprising fluidizing the hydrided and unhydrided metal materials in a gravity environment to achieve a separation based upon density differences.

10 . The method of claim 1 , further comprising separating the hydrided metal material from unhydrided metal material, comprising acid bath treatment under conditions where the hydrided metal material is not dissolved and unhydrided metal materials are dissolved.

11 . The method of claim 1 , wherein the metal-containing waste material includes at least one of titanium, zirconium and hafnium, further comprising:
separating one or more metals of the metal-containing waste material from other metals of the metal-containing waste material using a molten salt electrochemical process to obtain titanium, zirconium or hafnium; and annealing the metal-containing waste material.

12 . A method of recovering a metal from a metal-containing waste material, comprising:
imposing an electrochemical environment upon a metal oxide material in a basket of an electrochemical cell immersed in a molten salt electrolyte, the molten salt electrolyte comprising:
a CaCl 2 /CaO electrolyte composition, wherein the CaO constitutes between about 0.25 wt. % and about 5.0 wt. % of the molten salt electrolyte, and the CaCl 2 comprises up to 99.75 wt. % of the molten salt electrolyte,
a counter electrode of the electrochemical cell comprising a nonmetal selected from:
a ceramic selected from tin oxide, zinc ferrite, nickel ferrite, lithium ferrite and samarium ferrite;
a carbonaceous material;
a metal selected from palladium, ruthenium, and iridium; and

reducing the metal oxide material to a reduced metal in the molten salt electrolyte, wherein the reduced metal is selected from a transition metal, a refractory metal and a rare earth metal.

13 . The method of claim 12 , wherein the counter electrode comprises a metal selected from the group consisting of a glassy carbon, platinum, osmium, iridium, ruthenium, rhodium, palladium, silver, and gold.

14 . The method of claim 12 , prior to imposing an electrochemical environment upon a metal oxide material, the method further comprising:
heating a metal-containing waste material under a hydrogen flow to form a hydrided metal material; and removing hydrogen from the hydrided metal material to form an elemental metal or a metal oxide.

15 . The method of claim 12 , further comprising rinsing the reduced metal to remove residual electrolyte.

16 . The method of claim 12 , further comprising:
rinsing the reduced metal to remove residual electrolyte; and annealing the reduced metal wherein annealing is carried out under reducing conditions.

17 . An electrochemical cell, comprising:
a working electrode immersed in a molten salt electrolyte; the molten salt electrolyte comprising:
at least one of an alkali halide salt and an alkaline earth metal halide salt; a metal compound comprising an oxidized metal or a partially hydrided metal in a basket located within the molten salt electrolyte, wherein the working electrode is in electrochemical contact with the metal compound and the basket; a counter electrode immersed in the molten salt electrolyte, the counter electrode comprising at least one material selected from graphite, lithium iridate, lithium ruthenate, lithium rhodate, a tin oxide compound, a lithium tin oxygen compound, a lithium manganese oxygen compound, calcium ruthenate, a strontium ruthenium ternary compound, calcium iridate, strontium iridate, calcium platinate, strontium platinate, magnesium ruthenate, magnesium iridate, sodium ruthenate, sodium iridate, potassium iridate, potassium ruthenate, and nickel superalloys including rhenium containing nickel superalloys, ruthenium containing nickel superalloys, and rhenium-ruthenium nickel superalloys; a reference electrode, selected from glassy carbon, nickel, nickel/nickel oxide, silver/silver chloride, a platinum group metal, a precious metal, and combinations thereof; and an inert atmosphere.

18 . The electrochemical cell of claim 17 , wherein the molten salt electrolyte comprises a CaCl 2 /CaO electrolyte composition, wherein the CaO constitutes between about 0.25 wt. % and about 5.0 wt. % of the molten salt electrolyte, and the CaCl 2 comprises up to 99.75 wt. % of the molten salt electrolyte.

19 . The electrochemical cell of claim 17 , wherein:
the metal compound is selected from oxide compounds of scandium, titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, yttrium, zirconium, niobium, molybdenum, ruthenium, rhodium, palladium, silver, cadmium, lanthanum, hafnium, tantalum, tungsten, rhenium, osmium, iridium, platinum, gold, vanadium, cerium, dysprosium, erbium, europium, gadolinium, holmium, lanthanum, lutetium, neodymium, praseodymium, promethium, samarium, scandium, terbium, thulium, ytterbium, and yttrium.

20 . The electrochemical cell of claim 17 , wherein:
the metal compound is selected from partial hydrided compounds of scandium, titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, yttrium, zirconium, niobium, molybdenum, ruthenium, rhodium, palladium, silver, cadmium, lanthanum, hafnium, tantalum, tungsten, rhenium, osmium, iridium, platinum, gold, vanadium, cerium, dysprosium, erbium, europium, gadolinium, holmium, lanthanum, lutetium, neodymium, praseodymium, promethium, samarium, scandium, terbium, thulium, ytterbium, and yttrium.

Assignees

• Battelle Energy Alliance Llc

Inventors

• Tripathy Prabhat K

Classifications

• C25C3/26

  of titanium, zirconium, hafnium, tantalum or vanadium · CPC title

• C25C7/005

  of cells for the electrolysis of melts (C25C7/02 - C25C7/06 take precedence) · CPC title

• C25C3/28 Primary

  of titanium · CPC title

• Y02P10/20

  Recycling · CPC title