Method of manufacturing inorganic ion exchanger for the selective extraction of lithium from lithium-containing natural and technological brines
View Patent ↗Proposed is a method of manufacturing an inorganic ion exchanger with improved selectivity for lithium. The exchanger is represented by the following general formula: H a NbO (2.5+0.5·a) ·bLi 2 O·cWO 3 ·dH 2 O, wherein “a” is a number ranging from 0.5 to 2.0, “b” is a number ranging from 0.01 to 0.5, “c” is a number ranging from 0.01 to 0.2, and “d” is a number ranging from 0.1 to 2.0. The method consists of: interacting a soluble niobate (V) with an acid to form a hydrated niobium (V) oxide and a hydrated tungsten (VI) oxide, which co-precipitate and form a mixed hydrated niobium (V) and tungsten (VI) oxide; granulating the obtained product; converting the granulated product into a lithium form; calcining the lithium form to obtain a mixed granulated tripled lithium, niobium (V) and tungsten (VI) oxide, and converting the lithium-form into an H-form of the inorganic ion-exchanger by treating it with an acid solution.
1. A method of manufacturing inorganic ion exchanger for the selective extraction of lithium from lithium-containing natural and technological brines, the inorganic ion exchanger being represented by the following general formula:
H a NbO (2.5+0.5·a) ·bLi 2 O·cWO 3 ·dH 2 O;
wherein:
“a” is a number ranging from 0.5 to 2.0,
“b” is a number ranging from 0.01 to 0.5,
“c” is a number ranging from 0.01 to 0.2, and
“d” is a number ranging from 0.1 to 2.0, wherein the method comprising the following steps:
interacting a soluble niobate (V) with an acid that contains at least one soluble tungsten (VI) compound, thus forming a hydrated niobium (V) oxide and a hydrated tungsten (VI) oxide, which co-precipitate and form a mixed hydrated niobium (V) and tungsten (VI) oxide;
granulating the mixed hydrated niobium (V) and tungsten (VI) oxide by freezing with subsequent defreezing, thus obtaining a granulated mixed hydrated niobium (V) and tungsten (VI) oxide;
converting the granulated mixed hydrated niobium (V) and tungsten (VI) oxide into a lithium form by treating thereof with a lithium-containing compound selected from the group consisting of aqueous solutions of lithium hydroxide and lithium carbonate;
calcining the lithium form of the granulated mixed hydrated niobium (V) and tungsten (VI) oxide to obtain a mixed granulated tripled lithium, niobium (V) and tungsten (VI) oxide, which constitutes a lithium-form of the inorganic ion-exchanger; and
converting the lithium-form of the inorganic ion-exchanger into an H-form of the inorganic ion-exchanger by treating thereof with an acid solution.
2. The method of claim 1 , wherein the polymeric aqua-oxo-hydroxo complex is a polymeric aqua-oxo-hydroxo complex of niobium and tungsten in the form of solid particles.
3. The method of claim 2 , wherein the soluble niobate (V) is an alkali metal orthoniobate selected from the group consisting of Li 3 NbO 4 , Na 3 NbO 4 , K 3 NbO 4 , Rb 3 NbO 4 , Cs 3 NbO 4 .
4. The method of claim 1 , wherein the soluble tungsten (VI) compound is a monotungstate based on the WO 4 2− anion and selected from the group consisting of Li 2 WO 4 , Na 2 WO 4 , K 2 WO 4 , Rb 2 WO 4 , Cs 2 WO 4 , (NH 4 ) 2 WO 4 .
5. The method of claim 3 , wherein the soluble tungsten (VI) compound is a monotungstate based on the WO 4 2− anion and selected from the group consisting of Li 2 WO 4 , Na 2 WO 4 , K 2 WO 4 , Rb 2 WO 4 , Cs 2 WO 4 , (NH 4 ) 2 WO 4 .
6. The method of claim 1 , wherein the interaction of niobates with acid is carried out in the presence of a tungsten (VI) salt at an ionic ratio of niobium (V) to tungsten (VI) being in a range of 1 to (0.04 to 0.12).
7. The method of claim 1 , wherein the step of freezing is carried out for 24 to 48 hours at a temperature in a range of −4° C. to −10° C.
8. The method of claim 3 , wherein the step of freezing is carried out for 24 to 48 hours at a temperature in a range of −4° C. to −10° C.
9. The method of claim 4 , wherein the step of freezing is carried out for 24 to 48 hours at a temperature in a range of −4° C. to −10° C.
10. The method of claim 1 , wherein the step of calcining is carried out at a temperature in the range of 450° C. to 550° C.
11. The method of claim 3 , wherein the step of calcining is carried out at a temperature in the range of 450° C. to 550° C.
12. The method of claim 4 , wherein the step of calcining is carried out at a temperature in the range of 450° C. to 550° C.
13. The method of claim 7 , wherein the step of calcining is carried out at a temperature in the range of 450° C. to 550° C.
14. The method of claim 1 , wherein the step of converting the granulated mixed hydrated niobium (V) and tungsten (VI) oxide into a lithium form, is carried out with a solution of an acid selected from the group consisting of nitric (HNO 3 ), hydrochloric (HCl), sulfuric (H 2 SO 4 ) or perchloric acid (HClO 4 ).
15. The method of claim 2 , wherein the step of converting the granulated mixed hydrated niobium (V) and tungsten (VI) oxide into a lithium form, is carried out with a solution of an acid selected from the group consisting of nitric (HNO 3 ), hydrochloric (HCl), sulfuric (H 2 SO 4 ) or perchloric acid (HClO 4 ).
16. The method of claim 3 , wherein the step of converting the granulated mixed hydrated niobium (V) and tungsten (VI) oxide into a lithium form, is carried out with a solution of an acid selected from the group consisting of nitric (HNO 3 ), hydrochloric (HCl), sulfuric (H 2 SO 4 ) or perchloric acid (HClO 4 ).
17. The method of claim 11 , wherein the step of converting the granulated mixed hydrated niobium (V) and tungsten (VI) oxide into a lithium form, is carried out with a solution of an acid selected from the group consisting of nitric (HNO 3 ), hydrochloric (HCl), sulfuric (H 2 SO 4 ) or perchloric acid (HClO 4 ).