IP Library › Granted Patent US 10,550,014
Granted Patent B2
US 10,550,014 · App. 15/972,930 · Granted Feb 4, 2020

Electrochemical desalination system with coupled electricity storage

Inventors: Divyaraj Desai (Sunnyvale, CA); Eugene S. Beh (Portola Valley, CA); Armin R. Volkel (Mountain View, CA); Quentin L. C. Van Overmeere (Mountain View, CA); Jessica Louis Baker Rivest (Palo Alto, CA)
Assignee: Palo Alto Research Center Incorporated
C02F1/4604C02F1/46109H01M4/368H01M4/42H01M4/58H01M8/188C02F1/441C02F2001/46133C02F2101/12C02F2103/08C02F2201/4618C02F2201/46115
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Quick Facts
Patent No.
US 10,550,014
App. No.
15/972,930
Filed
May 7, 2018
Granted
Feb 4, 2020
Kind
B2
Art Unit
1724
USPC
429/111
Abstract

A desalination and energy storage system comprises at least one water reservoir, at least one negative-ion redox electrode, at least one positive-ion redox electrode, a cation-exchange membrane disposed between the at least one negative-ion redox electrode and the water reservoir, and an anion-exchange membrane disposed between the at least one positive-ion redox electrode and the water reservoir. The at least one water reservoir comprises an input and an output, wherein water in the at least one water reservoir is reduced below a threshold concentration during a desalination operation mode. The at least one negative-ion electrode comprises a first solution and is configured to accept, and have, a reversible redox reaction with at least one negative ion in the water, and the at least one positive-ion electrode comprises a second solution and is configured to accept, and have, a reversible redox reaction with at least one positive ion in the water.

Claims (45)

1. A reversible desalination and energy storage system, comprising:

at least one water reservoir comprising an input and an output, wherein water in the at least one water reservoir is reduced below a threshold concentration during a desalination operation mode;

at least one negative-ion redox electrode comprising a first solution of a first electrolyte material and configured to accept, and have a reversible redox reaction with, at least one negative ion in the water;

at least one positive-ion redox electrode comprising a second solution of a second electrolyte material and configured to accept, and have a reversible redox reaction with, at least one positive ion in the water;

a cation-exchange membrane disposed between the at least one negative-ion redox electrode and the water reservoir; and

an anion-exchange membrane disposed between the at least one positive-ion redox electrode and the water reservoir.

2. The system of claim 1 , wherein the system is configured to remove dissolved ionic species from the water in the at least one water reservoir having an electrolyte concentration of up to the solubility limit of the ionic species in the solution.

3. The system of claim 1 , wherein the system is configured to add dissolved ionic species to the water in the at least one water reservoir to provide an electrolyte concentration in the water of up to the solubility limit of the ionic species in the water.

4. The system of claim 1 , wherein the first solution, the second solution, and the water each has a pH between and including 3-10.

5. The system of claim 1 , wherein the system is configured to operate alternately in a desalination mode and a salination mode, wherein the salination mode comprises driving ions from the at least one negative-ion redox electrode and the at least one positive-ion redox electrode into the at least one water reservoir while storing energy in the system, and the desalination mode comprises desalinating water while releasing stored energy as output power employing the at least one negative-ion redox electrode as a positive or negative output electrode and the at least one positive-ion redox electrode as a negative or positive output electrode.

6. The system of claim 1 , wherein the system has a standard cell potential of at least 0.8 V.

7. The system of claim 1 , wherein the input water comprises seawater, and the output is brackish water having salinity of about 5 parts per thousand.

8. The system of claim 1 , further comprising a second desalination system coupled to the water reservoir output, wherein the second desalination system uses a water treatment process other than an electrochemical battery.

9. The system of claim 8 , wherein the second desalination system uses reverse osmosis.

10. The system of claim 8 , wherein the second desalination system is configured to output potable water.

11. An apparatus, comprising:

a first system according to claim 1 ; and

a second system according to claim 1 .

12. The apparatus of claim 11 , wherein the first system and the second system are configured to operate in a desalination mode and a salination mode, and the first and second system operate in the same mode at the same time.

13. The apparatus of claim 11 , wherein the first system and the second system are configured to operate in a desalination mode and a salination mode, and the first and second systems operate in different modes at the same time.

14. A method, comprising:

providing an electrochemical desalination battery unit comprising:

at least one water reservoir comprising an input and an output, wherein water in the at least one water reservoir is reduced below a threshold concentration during a desalination operation mode;

at least one negative-ion redox electrode comprising a first solution of a first electrolyte material and configured to accept, and have a reversible redox reaction with, at least one negative ion in the water;

at least one positive-ion redox electrode comprising a second solution of a second electrolyte material and configured to accept, and have a reversible redox reaction with, at least one positive ion in the water;

a cation-exchange membrane disposed between the at least one negative-ion redox electrode and the water reservoir; and

an anion-exchange membrane disposed between the at least one positive-ion redox electrode and the water reservoir;

transporting water having a first salinity into the water reservoir;

discharging the battery unit to provide water having a second salinity that is lower than the first salinity; and

removing the water having the second salinity from the battery unit.

15. The method of claim 14 , further comprising:

transporting the water having the second salinity into a second desalination system; and

desalinating the water to provide water having a third salinity that is lower than the second salinity.

16. The method of claim 15 , wherein the third salinity is equal to or less than 0.5 parts per thousand.

17. The method of claim 14 , further comprising:

in response to removing the water having the second salinity, transporting water having a fourth salinity into the water reservoir; and

charging the battery unit to provide water having a fifth salinity that is higher than the fourth salinity.

18. The method of claim 17 , wherein the fourth salinity is equal to about the first salinity.

19. A reversible desalination and energy storage system comprising:

a central reservoir comprising a first electrolyte solution, an input and an output, wherein the first electrolyte solution has a first pH;

at least one negative-ion redox electrode comprising a second electrolyte solution and configured to accept, and have a reversible redox reaction with, at least one negative ion in the first electrolyte solution, wherein the second electrolyte solution has a second pH;

at least one positive-ion redox electrode comprising a third electrolyte solution and configured to accept, and have a reversible redox reaction with, at least one positive ion in the first electrolyte solution, wherein the third electrolyte solution has a third pH and the first, second, and third pH is between and including 3-10;

a cation-exchange membrane disposed between the at least one negative-ion redox electrode and the central reservoir; and

an anion-exchange membrane disposed between the at least one positive-ion redox electrode and the central reservoir.

20. The system of claim 19 , wherein the system is configured to operate alternately in a desalination mode and a salination mode, wherein the salination mode comprises driving ions from the at least one negative-ion redox electrode and the at least one positive-ion redox electrode into the central reservoir while storing energy in the system, and the desalination mode comprises desalinating the first electrolyte solution while releasing stored energy as output power employing the at least one negative-ion redox electrode as a positive or negative output electrode and the at least one positive-ion redox electrode as a negative or positive output electrode.

Assignments (7)
TERMINATION AND RELEASE OF SECURITY INTEREST IN PATENTS RECORDED AT RF 064760/0389 Recorded Feb 13, 2024
From: CITIBANK, N.A., AS COLLATERAL AGENT
To: XEROX CORPORATION
Reel/Frame 068261/0001 →
SECURITY INTEREST Recorded Feb 13, 2024
From: XEROX CORPORATION
To: CITIBANK, N.A., AS COLLATERAL AGENT
Reel/Frame 066741/0001 →
SECURITY INTEREST Recorded Nov 20, 2023
From: XEROX CORPORATION
To: JEFFERIES FINANCE LLC, AS COLLATERAL AGENT
Reel/Frame 065628/0019 →
CORRECTIVE ASSIGNMENT TO CORRECT THE REMOVAL OF US PATENTS 9356603, 10026651, 10626048 AND INCLUSION OF US PATENT 7167871 PREVIOUSLY RECORDED ON REEL 064038 FRAME 0001. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Jun 28, 2023
From: PALO ALTO RESEARCH CENTER INCORPORATED
To: XEROX CORPORATION
Reel/Frame 064161/0001 →
SECURITY INTEREST Recorded Jun 22, 2023
From: XEROX CORPORATION
To: CITIBANK, N.A., AS COLLATERAL AGENT
Reel/Frame 064760/0389 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 20, 2023
From: PALO ALTO RESEARCH CENTER INCORPORATED
To: XEROX CORPORATION
Reel/Frame 064038/0001 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 7, 2018
From: DESAI, DIVYARAJ; BEH, EUGENE S.; VOLKEL, ARMIN R.; VAN OVERMEERE, QUENTIN L.C.; RIVEST, JESSICA LOUIS BAKER
To: PALO ALTO RESEARCH CENTER INCORPORATED
Reel/Frame 045734/0586 →
Continuity (2)
Provisional Application 62544199 · Aug 11, 2017
Related Publication 20190047880A1 · Feb 14, 2019
Cited By (10)
US 12,221,360 US 12,239,941 US 12,261,338 US 12,276,436 US 12,510,257 US 12,515,166 US 12,571,546 US 12,606,469 US 12,624,470 US 12,693,037