Selective separation of elements or commodities of interest in aqueous streams
US-2018119252-A1 · May 3, 2018 · US
US12270089B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12270089-B2 |
| Application number | US-202017628507-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 22, 2020 |
| Priority date | Jul 25, 2019 |
| Publication date | Apr 8, 2025 |
| Grant date | Apr 8, 2025 |
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The present invention relates to a method for extracting a refractory metal selected from Nb, Ta, Mo, W and V, from a solid material comprising the refractory metal in an oxidised form, the method using a layered double hydroxide, and the use of a layered double hydroxide for extracting or purifying a refractory metal selected from Nb, Ta, Mo, W and V.
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The invention claimed is: 1. A method for extracting a refractory metal M selected from Nb, Ta, Mo, W, V, or a mixture of at least two of said refractory metals, from a solid material comprising said refractory metal in an oxidized form, wherein said method comprises at least the following steps: i) a step of contacting said solid material with a first aqueous composition comprising a first layered double hydroxide which is insoluble in said first aqueous composition, said first layered double hydroxide containing interlayer anions A1n−, n being a positive integer, to form polyoxometallates of said refractory metal which are soluble in said first aqueous composition, said polyoxometallates having a negative charge q− such that q is a positive integer and q>n, ii) a first step of ion exchange in said first aqueous composition of said interlayer anions An—with said polyoxometallates from step i), to form a second layered double hydroxide which is insoluble in said first aqueous composition, and iii) a second step of ion exchange of said polyoxometallates with anions A2p− in a second aqueous composition comprising said anions A2p−, p being a positive integer, to form monomeric species of said refractory metal which are soluble in said second aqueous composition, said monomeric species having a negative charge m− such that m is a positive integer and m≤p. 2. The method as claimed in claim 1 , wherein the solid material is an ore, a concentrate, or a ground material resulting from waste electrical or electronic equipment. 3. The method as claimed in claim 1 , wherein the solid material is a material in the form of particles having an average size of less than 20 μm. 4. The method as claimed in claim 1 , wherein the first layered double hydroxide is a material in the form of particles having an average size of less than 20 μm. 5. The method as claimed in claim 1 , wherein the first aqueous composition has a pH selected in a range of from 3.5 to 12.5. 6. The method as claimed in claim 1 , wherein the second aqueous composition has a pH selected in a range of from 7 to 11. 7. The method as claimed in claim 1 , wherein the first layered double hydroxide is selected from layered double hydroxides conforming to the formula (I) below: [M′II1- x M″III x (OH)2] x +A1 n - x/n.s H2O, in which: M′II and M″III represent respectively divalent and trivalent metal cations, A1 is an n-valent interlayer anion selected from monovalent and divalent anions and selected from organic and inorganic anions, x, s, and n are positive numbers, x corresponds to the molar fraction of M″III/(M′II+M″III), and 0<x<1, M′II is selected from Ca2+, Mg2+, Mn2+, Fe2+, Co2+, Ni2+, Cu2+, and Zn2+, and M″III is selected from Al3+, Mn3+, Fe3+, Co3+, and Cr3+. 8. The method as claimed in claim 1 , wherein said method further comprises, between steps ii) and iii), a step ii1) of solid/liquid separation to recover the second layered double hydroxide in the form of a solid. 9. The method as claimed in claim 1 , wherein said method further comprises, after step iii), a step iv) of solid/liquid separation to recover the monomeric species of said refractory metal in solution. 10. The method as claimed in claim 9 , wherein said method further comprises, after step iv), a step v) of precipitation of the refractory metal in the form of an oxide from the monomeric species of said refractory metal in solution. 11. The method as claimed in claim 1 , wherein the mass ratio of the mass of said solid material to the mass of the first layered double hydroxide in step i) is from 1 to 100. 12. The method as claimed in claim 1 , wherein the refractory metal is selected from Nb, Ta, and a mixture thereof, and in that step i) comprises the following substeps: ia) an alkaline treatment of said solid material at a temperature of less than or equal to 550° C., and ib) the mixing of the treated material from substep ia) with the first layered double hydroxide in the first aqueous composition, said first aqueous composition having a pH selected in a range of from 10 to 12.5. 13. The method as claimed in claim 1 , wherein the refractory metal is selected from Nb, Ta, and a mixture thereof, and in that the second aqueous composition further comprises at least one complexing agent. 14. The method as claimed in claim 1 , wherein the refractory metal is selected from W, Mo, V, or a mixture of at least two of said metals, and in that the first aqueous composition further comprises a compound capable of forming heteropolyanions selected from phosphates and silicates, the pH of the first aqueous composition being selected in a range of from 3.5 to 10. 15. The method as claimed in claim 1 , wherein the concentration of solid matter in the first aqueous composition is from 1 to 400 g/l. 16. The method as claimed in claim 1 , wherein in step i), the solid material and the first layered double hydroxide are in the form of an mixture of solid particles dispersed in the first aqueous composition. 17. A method for extracting or purifying a refractory metal selected from Nb, Ta, Mo, W, V, said method implementing a first layered double hydroxide containing interlayer anions A1n−, n being a positive integer, and a mixture of at least two of said refractory metals, from a solid material comprising said refractory metal in an oxidized form, by a method as defined in claim 1 .
Obtaining molybdenum {(treatment or purification of solutions by adsorption on solids C22B3/24, by liquid-liquid extraction C22B3/26, by ion-exchange extraction C22B3/42; preparation of molybdenum involving liquid-liquid extraction, adsorption or ion-exchange C01G39/003)} · CPC title
Obtaining niobium or tantalum · CPC title
Obtaining vanadium · CPC title
Wet processes · CPC title
by ion-exchange extraction · CPC title
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