IP Library Granted Patent US 12,600,642
Granted Patent B2
US 12,600,642 · App. 18/295,443 · Granted Apr 14, 2026

Methods for extracting lithium from brines

Inventors: Peng Lu (Dhahran, SA); Pan Luo (Dhahran, SA)
Assignee: SAUDI ARABIAN OIL COMPANY
C01D15/08
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Quick Facts
Patent No.
US 12,600,642
App. No.
18/295,443
Granted
Apr 14, 2026
Kind
B2
Abstract

Methods for extracting lithium from brines may include evaporating at least a portion of a brine using a number of one or more solar evaporation ponds to form a first slurry. A first solid may be separated from the first slurry and combined with an amount of a first precipitation additive to form a second slurry. A first liquid may be separated from the second slurry and at least a portion of the first liquid may be evaporated in a solar evaporation pond to form a third slurry. A second liquid may be separated from the third slurry and combined with an amount of a second precipitation additive to form a fourth slurry. A second solid may be separated from the fourth slurry and rehydrated, forming a fifth slurry. About 90 wt % or more of a salt in a solid product separated from the fifth slurry may be lithium carbonate.

Claims (54)

1 . A method comprising:

determining a number of one or more solar evaporation ponds; an amount of a first precipitation additive comprising soda ash, slaked lime, or a combination thereof; and an amount of a second precipitation additive comprising soda ash, by using a geochemical prediction model given an initial composition of a brine;

evaporating at least a portion of the brine using the number of one or more solar evaporation ponds to form a first slurry;

wherein a concentration of magnesium in the brine is about 100 ppm to about 50,000 ppm and a concentration of lithium in the brine is about 0.01 ppm to about 5,000 ppm;

separating a first solid from the first slurry;

combining the first solid with the amount of the first precipitation additive to form a second slurry comprising magnesium hydroxide, magnesium carbonate, or a combination thereof;

separating a first liquid from the second slurry;

evaporating at least a portion of the first liquid in a solar evaporation pond to form a third slurry;

separating a second liquid from the third slurry;

combining the second liquid with the amount of the second precipitation additive to form a fourth slurry comprising lithium carbonate;

separating a second solid from the fourth slurry;

rehydrating the second solid to form a fifth slurry; and

separating a solid product from the fifth slurry, wherein about 90 wt % or more of a salt in the solid product is lithium carbonate.

2 . The method of claim 1 , wherein a ratio of total dissolved solids concentration to lithium concentration in the brine is about 1,500 ppm to about 1,000,000 ppm and a concentration of sodium in the brine is less than about 90,000 ppm.

3 . The method of claim 1 , wherein the geochemical prediction model is a Harvie-Møller-Weare model.

4 . The method of claim 1 , wherein the first precipitation additive further comprises caustic soda.

5 . The method of claim 1 , wherein the first slurry has a concentration of total dissolved solids of about 200,000 ppm to about 500,000 ppm.

6 . The method of claim 1 , wherein the third slurry has a concentration of total dissolved solids of about 200,000 ppm to about 1,000,000 ppm.

7 . The method of claim 1 , wherein the brine further comprises calcium, sodium, potassium, chloride, bicarbonate, sulfate, or any combination thereof.

8 . A method comprising:

determining a number of one or more solar evaporation ponds; an amount of a first precipitation additive comprising soda ash, slaked lime, or a combination thereof; and an amount of a second precipitation additive comprising soda ash, by using a geochemical prediction model given an initial composition of a brine;

evaporating at least a portion of the brine using the number of one or more solar evaporation ponds to form a first slurry;

wherein a concentration of magnesium in the brine is about 100 ppm to about 50,000 ppm and a concentration of lithium in the brine is about 0.01 ppm to about 5,000 ppm;

separating a first liquid from the first slurry;

combining the first liquid with the amount of the first precipitation additive to form a second slurry comprising magnesium hydroxide, magnesium carbonate, or a combination thereof;

separating a second liquid from the second slurry;

evaporating at least a portion of the second liquid in a solar evaporation pond to form a third slurry;

separating a third liquid from the third slurry;

combining the third liquid with the amount of the second precipitation additive to form a fourth slurry comprising lithium carbonate;

separating a first solid from the fourth slurry;

rehydrating the first solid to form a fifth slurry; and

separating a solid product from the fifth slurry, wherein about 90 wt % or more of a salt in the solid product is lithium carbonate.

9 . The method of claim 8 , wherein a ratio of total dissolved solids concentration to lithium concentration in the brine is about 1,500 ppm to about 1,000,000 ppm and a concentration of sodium in the brine is about 90,000 ppm to about 1,000,000 ppm.

10 . The method of claim 8 , wherein the geochemical prediction model is a Harvie-Møller-Weare model.

11 . The method of claim 8 , wherein the first precipitation additive further comprises caustic soda.

12 . The method of claim 8 , wherein the first slurry has a concentration of total dissolved solids of about 200,000 ppm to about 500,000 ppm.

13 . The method of claim 8 , wherein the third slurry has a concentration of total dissolved solids of about 200,000 ppm to about 1,000,000 ppm.

14 . The method of claim 8 , wherein the brine further comprises calcium, sodium, potassium, chloride, bicarbonate, sulfate, or any combination thereof.

15 . A method comprising:

determining a number of one or more solar evaporation ponds; an amount of a first precipitation additive comprising soda ash, slaked lime, or a combination thereof; and an amount of a second precipitation additive comprising soda ash, by using a geochemical prediction model given an initial composition of a brine;

evaporating at least a portion of the brine using the number of one or more solar evaporation ponds to form a first slurry;

wherein a concentration of magnesium in the brine is about 100 ppm to about 50,000 ppm and a concentration of lithium in the brine is about 0.01 ppm to about 5,000 ppm;

separating a first liquid from the first slurry;

combining the first liquid with the amount of the first precipitation additive to form a second slurry comprising magnesium hydroxide, magnesium carbonate, or a combination thereof;

separating a second liquid from the second slurry;

combining the second liquid with the amount of the second precipitation additive comprising soda ash to form a third slurry comprising lithium carbonate;

separating a first solid from the third slurry;

rehydrating the first solid to form a fourth slurry; and

separating a solid product from the fourth slurry, wherein about 90 wt % or more of a salt in the solid product is lithium carbonate.

16 . The method of claim 15 , wherein a ratio of total dissolved solids concentration to lithium concentration in the brine is less than about 1,500 ppm.

17 . The method of claim 15 , wherein the geochemical prediction model is a Harvie-Møller-Weare model.

18 . The method of claim 15 , wherein the first precipitation additive further comprises caustic soda.

19 . The method of claim 15 , wherein the first slurry has a concentration of total dissolved solids of about 200,000 ppm to about 500,000 ppm.

20 . The method of claim 15 , wherein the brine further comprises calcium, sodium, potassium, chloride, bicarbonate, sulfate, or any combination thereof.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 4, 2023
From: LU, PENG; LUO, PAN
To: SAUDI ARABIAN OIL COMPANY
Reel/Frame 063217/0875 →
Continuity (1)
Related Publication 20240336491A1 · Oct 10, 2024
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