IP Library › Granted Patent US 11,371,116
Granted Patent B2
US 11,371,116 · App. 16/490,243 · Granted Jun 28, 2022

Lithium extraction method

Inventors: Brian Haynes (New South Wales, AU); Jason Mann (New South Wales, AU)
Assignee: Novalith Technologies Pty Limited
C22B3/06C22B1/24C22B26/12
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Quick Facts
Patent No.
US 11,371,116
App. No.
16/490,243
Granted
Jun 28, 2022
Kind
B2
Abstract

According to the present invention there is provided a method for the extraction of lithium from one or more lithium-containing ores such as spodumene, the inventive method comprising the steps of: milling said ore/s to a predetermined average particle size; optionally calcining the milled ore; further optionally performing a secondary milling step; providing an aqueous suspension of the one or more lithium-containing ores at a predetermined solids concentration; subjecting the one or more lithium-containing ores to an aqueous extraction medium defined by a predetermined partial pressure of CO 2 , a predetermined extraction temperature, over a predetermined time; and obtaining technical grade lithium carbonate/lithium bicarbonate therefrom. Optional concentration and/or precipitation/purification steps may follow.

Claims (19)

1. A method for the extraction of lithium from one or more lithium-containing ores, said method comprising the steps of:

a) milling said one or more lithium-containing ores to a predetermined average particle size to provide a milled crude ore;

b) calcining said milled crude ore at a predetermined calcining temperature to obtain a calcined milled crude ore;

c) providing an aqueous medium comprising a suspension of the calcined milled crude ore, at a predetermined solids concentration;

d) subjecting said calcined milled crude ore to an acidic extraction medium defined by a predetermined partial pressure of CO 2 , a predetermined extraction temperature, over a predetermined time; and

e) obtaining technical grade lithium carbonate and/or lithium bicarbonate in solution from the extraction medium.

2. The method according to claim 1 , wherein the one or more lithium-containing ores comprise β-spodumene, or wherein the one or more lithium-containing ores consist essentially of β-spodumene.

3. The method according to claim 1 , wherein the predetermined calcining temperature is greater than about 900° C., thereby to convert α-spodumene to β-spodumene.

4. The method according to claim 1 , wherein said predetermined partial pressure of CO 2 is between about 0.1 and about 300 bar; and wherein said predetermined extraction temperature is between about 20° C. and about 350° C.

5. The method according to claim 1 , wherein said predetermined solids concentration is between about 0.1 and about 60% w/w.

6. The method according to claim 1 , wherein said predetermined average particle size is between about 0.1 μm and about 1000 μm.

7. The method according to claim 1 , wherein said predetermined time is between about 1 and about 1000 minutes.

8. The method according to claim 1 , giving a yield on an extracted lithium to crude lithium basis of between about 1% and about 99%.

9. The method according to claim 1 , wherein one or more impurities are extracted from said one or more lithium-containing ores; wherein said one or more impurities comprise Na, K, Mg, Ca, Mn, Fe, Al, and Si; and wherein each of said one or more impurities is present at a concentration between about 0.5% and about 40% of the lithium concentration on a molar basis.

10. The method according to claim 1 , further comprising a concentration step f), wherein the technical grade lithium carbonate obtained in solution from step e) is concentrated.

11. The method according to claim 10 , wherein said concentration step comprises: a concentrator, evaporation, reverse osmosis, electrodialysis, liquid-liquid extraction, selective adsorption solid state extraction or membrane separation.

12. The method according to claim 10 , wherein following said concentration step g), the lithium carbonate precipitates out of solution; and wherein the method further comprises a filtration step g), thereby to separate the precipitated lithium carbonate.

13. The method according to claim 1 , wherein the aqueous medium comprises water, one or more mineral acids, one or more organic acids, one or more alkaline salts, one or more ionic liquids, and combinations thereof.

14. The method according to claim 13 , wherein the one of more mineral acids are supplemented with a predetermined partial pressure of CO 2 between about 0.1 and about 300 bar.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 11, 2021
From: THE UNIVERSITY OF SYDNEY
To: KEMPLANT R&D PTY LIMITED
Reel/Frame 055232/0372 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 11, 2021
From: KEMPLANT R&D PTY LIMITED
To: NOVALITH TECHNOLOGIES PTY LTD
Reel/Frame 055234/0583 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 30, 2019
From: HAYNES, BRIAN; MANN, JASON
To: THE UNIVERSITY OF SYDNEY
Reel/Frame 050223/0410 →
Priority Claims (1)
AU 2017900694 · Mar 1, 2017 · national
Continuity (1)
Related Publication 20200071794A1 · Mar 5, 2020
Cited By (2)
US 12,241,171 US 12,431,552