Granted Patent B2

US 12,227,426 · App. 16/797,292 · Granted Feb 18, 2025

Inventors: John L. Featherstone (El Centro, CA); Paul J. Hanson (Imperial, CA); Michael J. Garska (Calipatria, CA); Charles R. Marston (Midland, MI)

Assignee: ILIAD IP COMPANY, LLC

C01D15/04B01D15/361C01D15/02C01D15/08

Abstract

Claims (27)

1. A process of recovering lithium from a brine, said process comprising the steps of:

a. producing a lithium-rich solution from said brine by sequentially circulating said brine through a plurality of process zones of a rotating or indexing manifold valve system, said brine comprising lithium, said manifold valve system comprising a plurality of ion exchange beds or columns containing a lithium selective adsorbent or resin; and

b. recovering lithium chloride, lithium hydroxide, lithium carbonate, or a combination thereof from said lithium-rich solution using an eluant solution comprising lithium chloride and water.

2. The process of claim 1 wherein said brine is a geothermal brine.

3. The process of claim 1 , prior to said step of producing said lithium-rich solution, further comprising the step of producing a clarified or polished brine from said brine, said clarified or polished brine comprising lithium.

4. The process of claim 3 wherein the step of producing said clarified or polished brine further comprises the steps of selectively removing impurities from said brine and/or selectively recovering one or more metals, minerals or a combination thereof from said brine.

5. The process of claim 4 wherein said step selectively removing impurities from said brine further comprises the steps of:

a. selectively removing at least iron and silica from said geothermal brine to form a substantially iron and silica free brine; and

b. selectively at least removing manganese and zinc from said substantially iron and silica free brine to form said clarified brine.

6. The process of claim 5 further comprising the step of selectively removing monovalent ions, divalent ions or both from said clarified brine to form said polished brine.

7. The process of claim 6 further comprising the step of selectively removing calcium, magnesium, boron, or a combination thereof from said clarified brine using an ion exchange circuit to form said polished brine.

8. The process of claim 1 wherein said step of producing said lithium-rich solution further comprises sequentially circulating said brine through said process zones of a continuous counter-current ion exchange circuit of said manifold valve system.

9. The process of claim 8 wherein fluid flow through said ion exchange circuit is controlled by pumping flow rates and a predetermined timing of rotation or indexing of said manifold valve system whereby said exchange beds or columns continually cycle through said process zones.

10. The process of claim 8 wherein said process zones of said continuous counter-current ion exchange circuit of said manifold valve system are configured in parallel, in series, or in combinations of parallel and series, flowing either in up flow or down flow modes.

11. The process of claim 1 further comprising the step of selectively converting said lithium chloride in said lithium-rich solution to said lithium carbonate, said lithium hydroxide, or both.

12. The process of claim 11 wherein said step of selectively converting said lithium chloride further comprises the steps of:

selectively converting said lithium chloride in said lithium-rich solution to lithium carbonate using a lithium carbonate crystallization process; and/or

selectively concentrating said lithium chloride in said lithium-rich solution using a solvent extraction process, and, selectively converting said lithium chloride in said lithium-rich solution to lithium hydroxide using electrolysis or chemical conversion.

13. The process of claim 12 further comprising the steps of:

selectively recovering said lithium carbonate from said lithium carbonate crystallization process; and

selectively converting said lithium carbonate to said lithium hydroxide.

14. The process of claim 1 wherein said lithium chloride selective absorbent or resin is a manufactured resin-based alumina imbibed adsorbent, a lithium alumina intercalates adsorbent, an alumina imbibed ion exchange resin, or an alumina-based adsorbent.

15. The process of claim 1 wherein said step recovering lithium chloride, lithium hydroxide, lithium carbonate, or a combination thereof from said lithium-rich solution further comprises the step of:

b. recovering lithium chloride, lithium hydroxide, lithium carbonate, or a combination thereof from said lithium-rich solution using said eluant solution comprising lithium and water at a concentration of up to about 1000 mg/kg lithium and at temperatures of about 5° C.to about 100° C.

16. The process of claim 3 wherein said brine has a temperature of about 229° F+23° F.

17. The process of claim 5 wherein said substantially iron and silica free brine has an iron concentration of less than about 5 ppm and a silica concentration of less than about 5 ppm.

18. The process of claim 5 wherein said clarified brine has a manganese concentration of less than about 10 ppm and a zinc concentration of less than about 5 ppm.

Assignments (2)

Continuity (4)

References Cited (367)