IP Library Granted Patent US 12668497
Granted Patent B2
US 12668497 · App. 18/255,418 · Granted Jun 30, 2026

Lithium carbonate production process and apparatus

Inventors: Amit Patwardhan (Wilmington, DE); Sandip Shinde (Wilmington, DE); Allen Wattenbarger (Wilmington, DE)
Assignee: US Borax Inc.
C01D15/08B01D9/0022B01D9/004C01D7/24C01D7/26B01D2009/0086C01P2006/80
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Quick Facts
Patent No.
US 12668497
App. No.
18/255,418
Granted
Jun 30, 2026
Kind
B2
Abstract

A method of forming lithium carbonate from a lithium-bearing solution including: evaporating the lithium-bearing solution to precipitate a first group of impurities; removing the first group of impurities to form a first purified solution; and performing a flash crystallisation step within a predetermined temperature range to crystallise a second group of impurities from the first purified solution; removing the second group of impurities from the first solution to form a second purified solution, wherein at least 90 wt % of lithium is recovered from the first purified solution; and reacting the second purified solution with a metal carbonate to form lithium carbonate of at least 90 wt % purity.

Claims (17)

1 . A method of forming lithium carbonate from a lithium bearing solution including:

removing a first group of impurities comprising calcium and sodium-containing salts from the lithium-bearing solution to form a first purified solution;

performing a crystallisation step by flash crystallization within a temperature range from 13° C. to 20° C. to crystallise a second group of impurities comprising sodium, potassium and boron-containing impurities from the first purified solution;

removing the second group of impurities from the first purified solution to form a second purified solution, wherein at least 95 wt % of lithium is recovered from the first purified solution;

reacting the second purified solution with a metal carbonate to form lithium carbonate of at least 95 wt % purity.

2 . The method of claim 1 , including a filtering step to remove the first group of impurities.

3 . The method of claim 1 , wherein the evaporating step forms a first purified solution having a lithium concentration of at least 3,000 ppm.

4 . The method of claim 1 , wherein the crystallisation step recovers at least 98 wt % of the lithium from the first purified solution.

5 . The method of claim 1 , wherein the crystallizing step is performed at a temperature from 13° C. to 17° C.

6 . The method of claim 1 , including a filtering step to remove the second group of impurities formed during the crystallisation step.

7 . The method of claim 1 , including a second crystallisation step to separate sodium and potassium-containing impurities from the first purified solution.

8 . The method of claim 1 , wherein the crystallizing step forms a second purified solution having a lithium concentration of at least 10,000 ppm.

9 . The method of claim 1 , wherein the reacting step involves reacting the second purified solution with sodium carbonate to form lithium carbonate.

10 . The method of claim 1 , wherein the reacting step forms lithium carbonate of at least 99 wt % purity.

11 . The method of claim 1 , including a step of removing calcium carbonate from the second purified solution before the reacting step.

12 . The method of claim 1 , including a recycling step which directs liquor from the reacting step to the crystallisation step.

13 . The method of claim 1 , including a step of refining the lithium carbonate to a purity of at least 95 wt %.