IP Library › Granted Patent US 12,509,781
Granted Patent B2
US 12,509,781 · App. 17/199,463 · Granted Dec 30, 2025

Integrated lithium production process

Inventors: Jonathan Lipp (Givat Avni, IL); Nadav Dobrin (Kefar Yona, IL)
Assignee: TENOVA ADVANCED TECHNOLOGIES LTD.
C25B1/16C22B3/26C22B3/32C22B26/12C25B1/50C25B9/19C25B15/08Y02P10/20
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Quick Facts
Patent No.
US 12,509,781
App. No.
17/199,463
Granted
Dec 30, 2025
Kind
B2
Abstract

A lithium hydroxide production process integrating a lithium stripping stage with a lithium hydroxide production process performed in a two-compartment electrolysis cell.

Claims (42)

1 . A method of producing an aqueous lithium-containing solution from a lithium-loaded organic medium, the method comprising:

(a) providing a two-compartment electrolysis cell having an anode, a cathode, and a membrane barrier disposed therebetween, said membrane barrier being permeable to lithium (Li + ) cations and to protons (H + );

(b) stripping the lithium-loaded organic medium by means of an aqueous stripping solution, to extract said lithium cations from the lithium-loaded organic medium into the aqueous stripping solution, producing an aqueous, lithium-containing intermediate solution along with a stripped organic medium;

(c) introducing said aqueous, lithium-containing intermediate solution into an anodic compartment of said two-compartment electrolysis cell, to form an anolyte;

(d) introducing an aqueous medium into a cathodic compartment of said two-compartment electrolysis cell to form a catholyte;

(e) operating said cell so as to:

(i) generate oxygen gas at said anode;

(ii) produce said protons (H + ) within said anolyte; and

(iii) generate hydrogen gas and hydroxide (OH − ) at said cathode;

and such that a portion of said lithium cations and a portion of said protons traverse said membrane barrier, whereby said protons react with said hydroxide to produce water in said catholyte;

(f) removing an aqueous product stream from said cathodic compartment, said product stream containing dissolved lithium hydroxide values; and

(g) recycling a discharge stream containing said anolyte, from said anodic compartment, for use in said stripping of the lithium-loaded organic medium;

the method further comprising:

(h) between steps (b) and (c), separating said lithium-containing aqueous intermediate solution from said stripped organic medium;

(i) returning said stripped organic medium to an extraction stage; and

(j) mixing an aqueous lithium-containing feed solution with said stripped organic medium, in said extraction stage, to produce said lithium-loaded organic medium;

wherein said discharge stream contains said lithium cations and said protons (H + ) in a molar ratio within a range of 100:1 to 1:1 of Li + to H + .

2 . The method of claim 1 , wherein the method is a continuous method.

3 . A method of producing an aqueous lithium-containing solution from a lithium-loaded organic medium, the method comprising:

(a) providing a two-compartment electrolysis cell having an anode, a cathode, and a membrane barrier disposed therebetween, said membrane barrier being permeable to lithium (Li + ) cations and to protons (H + );

(b) stripping the lithium-loaded organic medium by means of an aqueous stripping solution, to extract said lithium cations from the lithium-loaded organic medium into the aqueous stripping solution, producing an aqueous, lithium-containing intermediate solution along with a stripped organic medium;

(c) introducing said aqueous, lithium-containing intermediate solution into an anodic compartment of said two-compartment electrolysis cell, to form an anolyte;

(d) introducing an aqueous medium into a cathodic compartment of said two-compartment electrolysis cell to form a catholyte;

(e) operating said cell so as to:

(i) generate oxygen gas at said anode;

(ii) produce said protons (H + ) within said anolyte; and

(iii) generate hydrogen gas and hydroxide (OH − ) at said cathode;

and such that a portion of said lithium cations and a portion of said protons traverse said membrane barrier, whereby said protons react with said hydroxide to produce water in said catholyte;

(f) removing an aqueous product stream from said cathodic compartment, said product stream containing dissolved lithium hydroxide values; and

(g) recycling a discharge stream containing said anolyte, from said anodic compartment, for use in said stripping of the lithium-loaded organic medium;

the method further comprising:

(h) between steps (b) and (c), separating said lithium-containing aqueous intermediate solution from said stripped organic medium;

(i) returning said stripped organic medium to an extraction stage; and

(j) mixing an aqueous lithium-containing feed solution with said stripped organic medium, in said extraction stage, to produce said lithium-loaded organic medium;

wherein, within said lithium-containing intermediate solution, said lithium cations are a predominant cation;

wherein, within said lithium-containing intermediate solution, sulfate anions are a predominant anion; and

wherein said discharge stream contains said lithium cations (Li + ) and said protons (H + ) in a molar ratio within a range of 40:1 to 1:2.

4 . The method of claim 3 , wherein the method is a continuous method.

5 . The method of claim 3 , wherein said molar ratio is within a range of 10:1 to 1:2.

6 . The method of claim 5 , wherein the method is a continuous method.

7 . The method of claim 5 , wherein said molar ratio is at least 1:1.

8 . The method of claim 7 , wherein the method is a continuous method.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 10, 2025
From: LIPP, JONATHAN; DOBRIN, NADAV
To: TENOVA ADVANCED TECHNOLOGIES LTD.
Reel/Frame 072533/0099 →
Priority Claims (1)
GB 1602259 · Feb 8, 2016 · national
Continuity (2)
Continuation 16073795
Related Publication 20210198793A1 · Jul 1, 2021
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