Lithium purification and conversion

US2023088458A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2023088458-A1
Application numberUS-202218052647-A
CountryUS
Kind codeA1
Filing dateNov 4, 2022
Priority dateJul 30, 2021
Publication dateMar 23, 2023
Grant date

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  5. First independent claim

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Abstract

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Lithium recovery processes are described using vaporization and conversion techniques. A vaporizer can be used to concentrate lithium and precipitate impurities. A conversion process can be used to replace anions in lithium bearing streams by adding a second anion and precipitating lithium in a salt with the second anion. Rotary separation can be used to separate the precipitated lithium salt.

First claim

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We claim: 1 . A method of recovering lithium from a brine source, comprising: extracting lithium from the brine source using an adsorption/desorption process to form a lithium extract; concentrating the lithium extract during a concentration stage to yield a lithium concentrate stream, wherein the concentration stage includes using a series of membrane separations to separate a brine stream with high lithium concentration, as a non-permeating stream, from a brine stream with low lithium concentration, as a permeating stream. 2 . The method of claim 1 , wherein the permeating stream and non-permeating stream flow in a counter-current format. 3 . The method of claim 2 , wherein the permeating stream and non-permeating stream flow from membrane to membrane in opposite sequential orientations. 4 . The method of claim 1 , wherein the lithium concentrate stream is obtained from the non-permeating stream. 5 . The method of claim 1 , wherein concentrating the lithium extract also yields a dilute brine stream, obtained from the permeating stream. 6 . The method of claim 1 , wherein the extraction stage includes contacting a brine source stream 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 extract. 7 . The method of claim 6 , wherein concentrating the lithium extract also yields a dilute brine stream, obtained from the permeating stream and wherein the dilute brine stream is recycled for use as eluent stream and/or to the brine source stream. 8 . The method of claim 7 , comprising treating impurities of the dilute brine stream using an impurity removal process. 9 . The method of claim 1 , further comprising converting the lithium concentrate stream during a conversion stage, wherein lithium chloride from the lithium concentrate stream is converted to lithium carbonate and/or hydroxide. 10 . The method of claim 1 , wherein the concentration stage includes additional concentration operations. 11 . The method of claim 10 , including further concentrating lithium salt in the lithium concentrate stream using a vaporizer. 12 . A method of recovering lithium from a brine source, comprising: extracting lithium from the brine source using an adsorption/desorption process to form a lithium extract; concentrating the lithium extract during a concentration stage to yield a lithium concentrate, wherein the concentration stage includes using a membrane separation process with a plurality of membrane separations in series operated in counter-current format. 13 . The method of claim 12 , wherein the membrane separation process includes a permeating stream and a non-permeating stream flowing from membrane to membrane to membrane in opposite sequential orientations. 14 . The method of claim 13 , wherein the lithium concentrate stream is obtained from the non-permeating stream. 15 . The method of claim 13 , wherein a dilute brine stream is obtained from the permeating stream. 16 . The method of claim 12 , wherein the extraction stage includes contacting a brine source stream 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 extract. 17 . The method of claim 16 , wherein the membrane separation process includes a permeating stream and a non-permeating stream flowing from membrane to membrane to membrane in opposite sequential orientations, wherein a dilute brine stream is obtained from the permeating stream and wherein the dilute brine stream is recycled for use as eluent stream and/or to the brine source stream. 18 . The method of claim 17 , comprising treating impurities of the dilute brine stream using an impurity removal process. 19 . The method of claim 12 , further comprising converting the lithium concentrate stream during a conversion stage, wherein lithium chloride from the lithium concentrate stream is converted to lithium carbonate and/or hydroxide. 20 . The method of claim 12 , wherein the concentration stage includes additional concentration operations.

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What does patent US2023088458A1 cover?
Lithium recovery processes are described using vaporization and conversion techniques. A vaporizer can be used to concentrate lithium and precipitate impurities. A conversion process can be used to replace anions in lithium bearing streams by adding a second anion and precipitating lithium in a salt with the second anion. Rotary separation can be used to separate the precipitated lithium salt.
Who is the assignee on this patent?
Schlumberger Technology Corp
What technology area does this patent fall under?
Primary CPC classification C22B26/12. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Thu Mar 23 2023 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 3 related publications on this page (citations in our corpus or others sharing the same primary CPC).