Granted Patent B2

US 12,515,166 · App. 18/133,023 · Granted Jan 6, 2026

Inventors: Eugene S. Beh (Portola Valley, CA); Jessica Louis Baker Rivest (Palo Alto, CA); Michael Benedict (Palo Alto, CA); Elif Karatay (Mountain View, CA)

Assignee: Genesee Valley Innovations, LLC

B01D53/1425B01D53/263B01D61/422B01D61/44B01D61/461C02F1/4693H01M8/188H01M8/227B01D2313/28B01D2313/30B01D2313/345B01D2313/36B01D2313/50C02F2103/08C02F2303/10H01M2250/10

Abstract

Claims (24)

1 . A method for separating a solvent from a salt dissolved in the solvent, comprising:

providing an electrodialysis apparatus comprising:

a first reservoir comprising a first input and a first output, wherein the salt dissolved in the solvent in the first reservoir is reduced below a threshold concentration during an operation mode;

a second reservoir comprising a second input and a second output, wherein the salt dissolved in the solvent in the second reservoir increases in concentration during the operation mode;

a first electrode contacting a first aqueous solution of a first redox-active electrolyte material and configured to have a first reversible redox reaction with the first redox-active electrolyte material, and the first redox-active electrolyte material accepts a salt ion of the salt from the solvent in the first reservoir;

a second electrode contacting a second aqueous solution of a second redox-active electrolyte material and configured to have a second reversible redox reaction with the second redox-active electrolyte material, and drive a salt ion of the salt from the second redox-active electrolyte material into the solvent in the second reservoir, wherein at least one of the first and second redox-active electrolyte materials comprises a ferrocene derivative that is chemically stable in oxidized and reduced forms to reaction with oxygen gas;

a first type of membrane disposed between the first and second reservoirs;

a second type of membrane, different from the first type, disposed between the first electrode and the first reservoir and disposed between the second electrode and the second reservoir;

transporting solvent having a first concentration of dissolved salt into the first and second reservoirs;

operating the electrodialysis apparatus to generate a first stream having a second concentration of the dissolved salt that is lower than the first concentration of the dissolved salt and to generate a second stream having a third concentration of the dissolved salt that is higher than the first concentration of the dissolved salt; and

transporting the first stream through a switching unit to a further desalination system to generate a further stream having a final concentration of the dissolved salt that is lower than second concentration of the dissolved salt, wherein the further desalination system uses a solvent treatment process different from the electrodialysis apparatus.

2 . The method according to claim 1 , wherein the first aqueous solution and the second aqueous solution are the same and the first and second aqueous solutions are circulated between the first electrode and the second electrode during the operation mode and the electrodialysis apparatus operates in an electrodialysis mode.

3 . The method according to claim 1 , wherein the first aqueous solution is an anolyte and the second aqueous solution is a catholyte, and the anolyte and the catholyte are different chemical species.

4 . The method according to claim 3 , wherein the electrodialysis apparatus operates in a charge mode or a discharge mode.

5 . The method according to claim 3 , wherein the electrodialysis apparatus operates alternately between a charge mode and a discharge mode.

6 . The method according to claim 1 , further comprising operating the electrodialysis apparatus in a discharge mode to generate power and powering at least a portion of the further desalination system with the power generated from the electrodialysis apparatus.

7 . The method according to claim 1 , wherein the switching unit is coupled to the first and second outputs of the first and second reservoirs and at least one output of the switching unit is coupled to the input of the further desalination system.

8 . The method according to claim 1 , wherein the further desalination system is a reverse osmosis system.

9 . The method according to claim 1 , wherein the further desalination system is a thermal evaporation system.

10 . The method according to claim 1 , wherein the further desalination system is a capacitive deionization system.

11 . The method according to claim 1 , wherein the final concentration of the dissolved salt is less than 0.5 ppt.

12 . The method according to claim 1 , wherein the further desalination system is coupled to a second electrodialysis apparatus through the switching unit.

13 . The method according to claim 12 , further comprising powering at least a portion of the further desalination system with power generated from the electrodialysis apparatus.

14 . The method according to claim 12 , wherein the first concentration of dissolved salt is about 35 ppt, and the final concentration of the dissolved salt is about 0.5 ppt.

Assignments (5)

Continuity (4)

References Cited (141)