Forward osmosis composite membranes for concentration of lithium containing solutions
US-2020047124-A1 · Feb 13, 2020 · US
US2023088458A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2023088458-A1 |
| Application number | US-202218052647-A |
| Country | US |
| Kind code | A1 |
| Filing date | Nov 4, 2022 |
| Priority date | Jul 30, 2021 |
| Publication date | Mar 23, 2023 |
| Grant date | — |
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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.
Opening claim text (preview).
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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