Granted Patent B2

US 12,257,529 · App. 18/476,195 · Granted Mar 25, 2025

Inventors: David Henry Snydacker (San Francisco, CA); Nicolás Andrés Grosso Giordano (Oakland, CA); Amos Indranada (Oakland, CA); Alysia Lukito (Emeryville, CA); Sean Utan (Oakland, CA); Mustafa Juzer Bootwala (Oakland, CA); Daniel Keane Laporte (Menlo Park, CA); Andrew Bolt Barber (San Francisco, CA); Christina Fleming (Naperville, IL); Garrett Lau (Castro Valley, CA)

Assignee: LILAC SOLUTIONS, INC.

B01D15/22B01D15/10B01D15/203B01D15/361B01D15/362B01D25/164B01D25/302B01J39/02B01J39/10B01J47/018B01J47/022B01J49/06B01J49/57B01J49/60C01D15/00C22B3/06C22B3/22C22B3/42C22B3/44C22B26/12B01D2251/302B01D2259/4146B01D2313/40

Abstract

Claims (22)

1. A process for extracting lithium from a liquid resource comprising:

a) contacting a lithium selective sorbent with the liquid resource, wherein the liquid resource comprises lithium ions, and wherein lithium ions in the liquid resource are at least partially absorbed by the lithium selective sorbent to yield an enriched lithium selective sorbent;

b) contacting said enriched lithium selective sorbent with an eluent such that lithium is at least partially eluted from said enriched lithium selective sorbent to yield an enriched eluate and the lithium selective sorbent; and

c) contacting an alternate phase with said lithium selective sorbent, said enriched lithium selective sorbent, said liquid resource, said eluent, said enriched eluate, or any combination thereof, wherein the alternate phase is a non-aqueous liquid or a gas.

2. The process of claim 1 , wherein the alternate phase of c) at least partially removes the liquid resource from the lithium selective sorbent and/or the enriched lithium selective sorbent following a).

3. The process of claim 1 , further comprising contacting at least one of the lithium selective sorbent and the enriched lithium selective sorbent with a wash solution.

4. The process of claim 3 , wherein the wash solution contacts the lithium selective sorbent and/or the enriched lithium selective sorbent after the alternate phase has contacted the lithium selective sorbent and/or the enriched lithium selective sorbent, and wherein a reduced amount of the wash solution is required to at least partially remove the liquid resource, the eluent, or the enriched eluate, from the surface of the lithium selective sorbent or the enriched lithium selective sorbent as compared to the process without the use of an alternate phase.

5. The process of claim 3 , wherein the alternate phase at least partially removes the wash solution from the lithium selective sorbent and/or the enriched lithium selective sorbent.

6. The process of claim 1 , wherein said alternate phase comprises an organic liquid or a gas,

wherein the organic liquid comprises an alkane, alcohol, ester, ether, oil, or any combination thereof, and

wherein the gas comprises air, nitrogen, argon, or any combinations thereof.

7. The process of claim 6 , wherein the alternate phase is a gas, and wherein the gas is injected at a pressure of 0.01-1000 psig.

8. The process of claim 1 , wherein said alternate phase comprises a gas, wherein the gas comprises air, nitrogen, argon, or any combinations thereof.

9. The process of claim 1 , wherein lithium extraction occurs in one or more vessels, wherein the one or more vessels comprise i) said lithium selective sorbent housed in a bed and ii) one or more ports for the addition of said liquid resource, said eluent, and said alternate phase.

10. The process of claim 9 , wherein the one or more vessels comprises one or more filter banks, and wherein the at least two or more filter banks are aligned in series to form a filter press.

11. The process of claim 1 , wherein said lithium selective sorbent and/or said enriched lithium selective sorbent is housed in one or more packed beds.

12. The process of claim 11 , wherein contacting the liquid resource and/or the enriched eluate with the alternative phase reduces the time required for the liquid resource and/or the enriched eluate to drain from the one or more packed beds.

13. The process of claim 1 , wherein said liquid resource contacts said lithium selective sorbent in a plurality of compartments arranged within a vessel.

14. The process of claim 1 , wherein said lithium selective sorbent is a protonated ion exchange material and the enriched lithium selective sorbent is a lithiated ion exchange material.

15. The process of claim 14 , wherein said protonated ion exchange material is generated by treating a pre-activated ion exchange material with an acid.

16. The process of claim 15 , wherein said pre-activated ion exchange material comprises LiFePO 4 , LiMnPO 4 , Li 2 TiO 3 , Li 2 MnO 3 , Li 2 SnO 3 , Li 4 Ti 5 O 12 , Li 4 Mn 5 O 12 , LiMn 2 O 4 , Li 1.6 Mn 1.6 O 4 , LiAlO 2 , LiCuO 2 , LiTiO 2 , Li 4 TiO 4 , Li 2 TinO 24 , Li 3 VO 4 , Li 2 Si 3 O 7 , Li 2 CuP 2 O 7 , modifications thereof, solid solutions thereof, or a combination thereof.

17. The process of claim 1 , wherein said lithium selective sorbent is an adsorbent, wherein the adsorbent comprises a crystalline lithium salt aluminate, a lithium aluminum intercalate, LiCl·2Al(OH) 3 , crystalline aluminum trihydroxide (Al(OH) 3 ), gibbsite, beyerite, nordstrandite, alumina hydrate, bauxite, amorphous aluminum trihydroxide, activated alumina layered lithium-aluminum double hydroxides, Li Al 2 (OH) 6 Cl, combinations thereof, compounds thereof, or solid solutions thereof.

Assignments (1)

Continuity (4)

References Cited (350)