Method of recovering lithium from a lithium source

Patent metadata

Field	Value
Publication number	US-2025177923-A1
Application number	US-202418965400-A
Country	US
Kind code	A1
Filing date	Dec 2, 2024
Priority date	Dec 1, 2023
Publication date	Jun 5, 2025
Grant date	—

Abstract

Described herein are methods of recovering lithium from dilute lithium sources. The methods include extracting lithium from an extraction feed using direct lithium extraction in an extraction stage to yield a lithium intermediate, performing one or more concentration operations, each concentration operation concentrating an input stream to yield an output feed, wherein the input stream is obtained from the lithium intermediate and/or the extraction feed is obtained from the output feed. At least one of the concentration operations includes a membrane separation operation having a plurality of reactors in series each having a semi-permeable membrane, such as a counter-flow reverse osmosis operation. Methods may also include generating a low TDS stream as a permeate from any of the one or more concentration operations, wherein the low TDS stream is recycled or used as fresh water.

First claim

We claim:

1 . A method of recovering lithium from a lithium source, comprising:
a. treating an aqueous source or a derivative thereof to yield a purified lithium intermediate, wherein treating the aqueous source or the derivative thereof includes:
i. extracting lithium from the aqueous source or derivative thereof using direct lithium extraction in an extraction stage,
ii. purifying the aqueous source or derivative thereof, in a purification stage,
b. in a post-extraction concentration stage, concentrating the purified lithium intermediate or a derivative thereof to yield a lithium concentrate, and c. in a monovalent impurity stage, removing monovalent impurities from the lithium concentrate or a derivative thereof to yield a purified lithium concentrate.

2 . The method of claim 1 , wherein the extraction stage employs an electrochemical separation method, a solvent extraction method, an ion withdrawal method, a membrane separation method, or a combination thereof.

3 . The method of claim 1 , further including converting lithium in the purified lithium concentrate into a lithium product.

4 . The method of claim 1 , wherein the monovalent impurity stage includes solids removal, crystallization, atomization, or any combination thereof.

5 . The method of claim 4 , wherein the monovalent impurity stage includes atomizing the lithium concentrate or derivative thereof to form a flow of humid air, heating the flow of humid air to form a flow of heated humid air and directing the flow of heated humid air into a cyclonic separator configured to precipitate monovalent impurities without precipitating lithium.

6 . The method of claim 4 , wherein the monovalent impurity stage includes a crystallization stage that circulates the lithium concentrate or derivative thereof into a porous fiber having an hydrophilic core and an hydrophobic surface.

7 . The method of claim 1 , further comprising routing the purified lithium concentrate or a derivative thereof to a conversion stage that converts lithium chloride of the purified lithium concentrate or derivative thereof into lithium hydroxide, lithium carbonate, or both.

8 . The method of claim 7 , wherein converting the lithium in the purified lithium concentrate into a lithium product uses an electrochemical process.

9 . The method of claim 1 , wherein the purification stage removes divalent impurities, transition metals, silica, sulfate ions, boron, organics, or a combination thereof.

10 . The method of claim 1 , wherein the purification stage includes solids removal, a selective impurity extraction process, a chemical process, or a combination thereof.

11 . The method of claim 1 , wherein concentrating the purified lithium intermediate or derivative thereof uses a membrane operation, an evaporation operation, or a combination thereof.

12 . The method of claim 1 , wherein concentrating the purified lithium intermediate or derivative thereof uses a reverse osmosis operation upstream of a counter-flow reverse osmosis operation, wherein the reverse osmosis separates the purified lithium intermediate or a derivative thereof into a preconcentrated stream and a permeate stream using a semi-permeable membrane.

13 . The method of claim 12 , wherein the counter-flow reverse osmosis operation includes flowing the preconcentrated stream or a derivative thereof into a plurality of reactors in series, each containing a semi-permeable membrane separating the reactor into a first volume and a second volume, wherein the preconcentrated stream flows as a first stream sequentially into the first volume of each reactor and a second stream flows sequentially into the second volume of each reactor counter-current to the first stream, wherein the first stream exiting the plurality of reactors yields a concentrated stream and the second stream exiting the plurality of reactors yields a dilute brine stream.

14 . The method of claim 13 , wherein the second stream is a portion of the concentrated stream.

15 . The method of claim 12 , wherein the one or more concentration operations includes a membrane distillation operation downstream of the counter-flow reverse osmosis operation, wherein the concentrated stream or a derivative thereof is directed to the membrane distillation operation.

16 . The method of any of claim 1 , wherein concentrating the purified lithium intermediate or derivative thereof uses a membrane distillation operation downstream of a non-thermal membrane separation operation that includes forward osmosis, reverse osmosis, osmotically assisted reverse osmosis, counter-flow reverse osmosis, pressure retarded osmosis, membrane pervaporation, or a combination thereof.

17 . The method of claim 1 , wherein the post-extraction concentration stage and the monovalent impurity stage together comprise two post-extraction concentration stages with intermediate monovalent removal stages.

18 . The method of claim 1 , wherein the extraction stage yields a lithium intermediate from the aqueous source or a derivative thereof and wherein the purification stage yields the purified lithium intermediate from the lithium intermediate.

19 . The method of claim 1 , wherein the extraction stage employs an adsorption-desorption process.

20 . The method of claim 1 , further comprising returning a removed stream of the purification stage, the concentration stage, the monovalent impurity removal stage, or a combination thereof, to any of the extraction stage, the purification stage, the concentration stage, the monovalent impurity removal stage, or a combination thereof.

21 . The method of claim 2 , further including converting lithium in the purified lithium concentrate into a lithium product.

Assignees

• Schlumberger Technology Corp

Inventors

• Binet Florence
• Aghajani Masoud
• Perroni Dominic Vincent
• Sams Gary Wayne
• Nirgudkar Prasanna
• Shampine Rod William
• Verma Sandeep
• Zhang Wenlin

Classifications

• Y02P10/20

  Recycling · CPC title

• B01D11/0492

  Applications, solvents used · CPC title

• B01D9/0059

  General arrangements of crystallisation plant, e.g. flow sheets · CPC title

• B01D9/0054

  Use of anti-solvent · CPC title

• B01D9/0031

  by heating (B01D9/0022, B01D9/0027 take precedence) · CPC title