Lithium recovery using aqueous sources

Patent metadata

Field	Value
Publication number	US-2025281850-A1
Application number	US-202519212744-A
Country	US
Kind code	A1
Filing date	May 20, 2025
Priority date	May 4, 2022
Publication date	Sep 11, 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:
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; wherein at least one of the concentration operations includes a counter-flow reverse osmosis operation, 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.

2 . The method of claim 1 , wherein one or more concentration operations include a reverse osmosis operation upstream of a counter-flow reverse osmosis operation, wherein the reverse osmosis separates the input stream into a preconcentrated stream and a permeate stream using a semi-permeable membrane, wherein the permeate stream is the low TDS stream.

3 . The method of claim 1 , wherein the counter-flow reverse osmosis operation includes flowing the preconcentrated stream 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 non-permeating stream sequentially into the first volume of each reactor and a permeating stream flows sequentially into the second volume of each reactor counter-current to the non-permeating stream, wherein the non-permeating stream exiting the plurality of reactors yields a concentrated stream and the permeating stream exiting the plurality of reactors yields a dilute brine stream.

4 . The method of claim 3 , wherein the dilute brine stream is recycled into the reverse osmosis operation.

5 . The method of claim 1 , wherein the at least one concentration operation includes a feed preparation operation, wherein the input stream is an aqueous lithium source and the output feed is the extraction feed.

6 . The method of claim 1 , wherein the at least one concentration operation includes concentrating a stream derived from the lithium intermediate as the input stream to yield a lithium concentrate as the output feed.

7 . The method of claim 1 , wherein at least a portion of the low TDS stream is recycled into the extraction stage.

8 . The method of claim 1 , wherein extracting lithium from the extraction feed includes contacting the extraction feed with a lithium selective medium to load the medium with lithium and contacting an eluent stream with the lithium-loaded medium to form the lithium intermediate, wherein the low TDS stream is recycled into the eluent stream.

9 . A method of recovering lithium from a lithium source, comprising:
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; wherein the at least one concentration operations includes
a first membrane separation operation, having a first semi-permeable membrane, yielding from the input stream a preconcentrated stream and a permeate stream,
a second membrane separation operation, wherein the preconcentrated stream flows 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 sequentially as a non-permeating stream into the first volume of each reactor, wherein the non-permeating stream exiting the plurality of reactors yields the output stream, and wherein the second membrane separation operation yields a dilute brine stream that exits the second volume of at least one of the reactors, wherein the dilute brine stream is recycled into the first membrane separation operation.

10 . The method of claim 9 , wherein the second membrane separation operation includes a permeating stream that flows sequentially into the second volume of the plurality of reactors, counter-current to the permeating stream, wherein at least a portion of the non-permeating stream is recycled into the permeating stream, wherein the permeating stream yields the dilute brine stream.

11 . The method of claim 9 , wherein the at least one concentration operation include a feed preparation operation that concentrates the aqueous lithium source to yield the extraction feed.

12 . The method of claim 9 , wherein the at least one concentration operation includes concentrating a stream derived from the lithium intermediate to yield a lithium concentrate.

13 . The method of claim 9 , wherein at least a portion of the permeate stream is recycled into the extraction stage.

14 . A method of recovering lithium from a brine source, comprising:
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; wherein the at least one concentration operations includes at least a membrane separation operation, wherein at least one the membrane separation operation includes a plurality of reactors in series each having a semi-permeable membrane, yields a lithium concentrate and a dilute brine stream, and is configured so that the lithium concentrate has a TDS over 120,000 mg/l, preferably over 200,000 mg/l, separating the dilute brine stream using a semi-permeable membrane into two streams including a permeate stream, wherein the permeate stream has a TDS under 2,000 mg/l, preferably under 500 mg/l, recycling the permeate stream.

15 . The method of claim 14 ,
wherein the one or more concentration operations include:
a first membrane separation operation yielding a preconcentrated stream and a diluted stream from the input stream,
a second membrane operation, wherein the at least one membrane separation is the second membrane operation,
and the method includes providing the dilute brine stream into the first membrane separation operation, wherein the diluted stream is the permeate stream.

16 . The method of claim 14 , wherein, in the second membrane separation operation, each semi-permeable membrane separate the associated reactor into a first volume and a second volume, wherein a stream derived from the input stream flows sequentially as a non-permeating stream into the first volume of each reactor, and wherein the dilute brine stream that exits the second volume of at least one of the reactors, wherein the dilute brine stream is recycled into the first membrane separation operation.

17 . The method of claim 16 , wherein the second membrane separation operation includes a permeating stream that flows sequentially into the second volume of the plurality of reactors, counter-current to the permeating stream, wherein at least a portion of the non-permeating stream is recycled into the permeating stream, wherein the permeating stream yields the dilute brine stream.

18 . The method of claim 14 , wherein the at least one concentration operation include a fee

Assignees

• Schlumberger Technology Corp

Inventors

• Sams Gary W
• Perroni Dominic Vincent
• Nirgudkar Prasanna
• Binet Florence
• Shampine Rod William

Classifications

• C22B3/24

  by adsorption on solid substances, e.g. by extraction with solid resins · CPC title

• C25C1/02

  of light metals · CPC title

• C22B3/22

  by physical processes, e.g. by filtration, by magnetic means {, or by thermal decomposition} (treatment or purification of solutions by liquid-liquid extraction C22B3/26) · CPC title

• C22B26/12 Primary

  Obtaining lithium · CPC title

• B01D2317/022

  Reject series · CPC title