Granted Patent B2

US 12,341,228 · App. 18/774,490 · Granted Jun 24, 2025

Inventors: Rahul S. Nana (Panama City, FL); Rafael A. Feria (Pickens, SC)

H01M8/227B01D5/006B01D53/18B01D61/0022B01D61/005B01D61/364B01D61/46B01D69/02C25B1/04C25B9/65H01M8/04029H01M8/0693H02N11/002B01D2313/221B01D2313/502B01D2325/38

Abstract

Claims (72)

1. A salt gradient heat engine system comprising:

a reverse electrodialysis battery comprising:

an anode;

a cathode;

a first cell configured to cause a voltage difference between the anode and the cathode, the first cell comprising:

a first membrane configured to be selectively permeable to cations;

a second membrane configured to be selectively permeable to anions, the second membrane being spaced apart from the first membrane to define a space between the first membrane and the second membrane; and

a concentrated saline solution disposed in the space between the first membrane and the second membrane, the first and second membranes being configured to separate the concentrated saline solution from a dilute saline solution such that the first membrane selectively allows cations to pass through, thus increasing positive charge at the cathode and the second membrane selectively allows anions to pass through, thus increasing negative charge at the anode, causing a voltage difference between the cathode and the anode; and

a thermal optimization system configured to transfer thermal energy to at least one of the concentrated saline solution and the dilute saline solution;

a regeneration system selected from the group consisting of: a salt precipitation system, a membrane distillation system, an evaporation system, a forward osmosis system, a salt decomposition system, an electrodialysis system, and any combination thereof, and

a second cell, the second cell comprising:

a third membrane configured to be selectively permeable to cations;

a fourth membrane configured to be selectively permeable to anions, the fourth membrane spaced apart from the third membrane; and

a second concentrated saline solution disposed between the third membrane and the fourth membrane, the third and fourth membranes separating the second concentrated saline solution from a second dilute saline solution, wherein:

the concentrated saline solution comprises an endothermic solution;

the second concentrated saline solution comprises an exothermic solution; and

a heat pump configured to transfer heat between the concentrated saline solution and the second concentrated saline solution.

2. The salt gradient heat engine system of claim 1 , wherein the regeneration system further comprises a dilute tank configured to receive a spent dilute solution from the reverse electrodialysis battery and to receive water from a switchable solubility system, wherein the water mixes with the spent dilute solution to regenerate the dilute saline solution.

3. The salt gradient heat engine system of claim 2 , wherein the switchable solubility system comprises:

a draw solution to be circulated through the forward osmosis system and produce a spent draw solution;

a recovery configured to receive the spent draw solution and add heat, wherein CO 2 is released and water is produced; and

a generator configured to receive the solution from the recovery and add CO 2 to regenerate the draw solution.

4. Method of generating electricity, the method comprising:

adding heat to, or removing heat from a concentrated saline solution or a dilute saline solution of a reverse electrodialysis battery, wherein a difference between salinity of the concentrated saline solution and the dilute saline solution defines a salinity gradient, the reverse electrodialysis battery comprising:

an anode;

a cathode;

one or more cells configured to cause a voltage difference between the anode and the cathode, at least one of the one or more cells comprising:

a first membrane configured to be selectively permeable to cations;

a second membrane configured to be selectively permeable to anions, the second membrane being spaced apart from the first membrane to define a space between the first membrane and the second membrane; and

the concentrated saline solution being disposed in the space between the first membrane and the second membrane, the first and second membranes being configured to separate the concentrated saline solution from the dilute saline solution such that the first membrane selectively allows cations to pass through, thus increasing positive charge at the cathode and the second membrane selectively allows anions to pass through, thus increasing negative charge at the anode, causing a voltage difference between the cathode and the anode; and

a thermal optimization system configured to transfer thermal energy to at least one of the concentrated saline solution and the dilute saline solution; and

regenerating the salinity difference between the dilute saline solution and the concentrated saline solution using a regeneration system comprising a forward osmosis system configured to receive a spent concentrated solution from the reverse electrodialysis battery, and regenerate the concentrated saline solution using a switchable solubility system.

5. The method of claim 4 , further comprising:

generating a third saline solution by membrane distillation; and

mixing the third saline solution into the concentrated saline solution and/or the dilute saline solution.

6. The method of claim 4 , further comprising using a portion of the generated electricity to produce hydrogen gas through electrolysis.

7. A method of generating electrical power from thermal energy, the method comprising:

separating, by a first selectively permeable membrane, a first saline solution from a second saline solution, wherein a difference between salinity of the first saline solution and the second saline solution defines a salinity gradient;

separating, by a second selectively permeable membrane, a third saline solution from a fourth saline solution, wherein the first saline solution comprises an endothermic solution and the third saline solution comprises an exothermic solution;

transferring, by a heat pump, thermal energy between the first saline solution and the third saline solution;

mixing the first saline solution and the second saline solution in a controlled manner, capturing at least some salinity-gradient energy as electrical power as the salinity difference between the first saline solution and the second saline solution decreases; and

regenerating the salinity difference between the first saline solution and the second saline solution by applying a regeneration process selected from the group consisting of: salt decomposition, electrodialysis, membrane distillation, evaporation, forward osmosis, or any combination thereof.

8. The method of claim 7 , wherein the method includes generating a third saline solution by membrane distillation, and further comprises mixing the third saline solution into the first saline solution and/or the second saline solution.

9. The method of claim 7 , wherein transferring thermal energy from the first saline solution to the second saline solution causes the first saline solution to precipitate a salt.

10. The method of claim 9 , further comprising introducing the precipitated salt into the second saline solution, causing the salinity difference between the first saline solution and the second saline solution to increase.

11. The method of claim 7 , further comprising using a portion of the generated electricity to produce hydrogen gas through electrolysis.

12. The method of claim 7 , wherein the regeneration process comprises applying the process of salt decomposition comprising:

i) providing a spent dilute solution formed from the first saline solution, wherein the spent dilute solution contains a salt;

ii) heating the spent dilute solution to decompose the salt to make a gaseous product; and

iii) transferring the gaseous product to an absorber; and

iv) solidifying the gaseous product to reform as a salt precipitate in a spent concentrate solution within the absorber;

wherein the salt precipitate dissolves in the spent concentrate solution to regenerate the second saline solution.

13. The method of claim 12 , wherein the spent dilute solution has a greater salinity than the first saline solution; and

wherein by transferring the gaseous product to the absorber, the salinity of the spent dilute solution is decreased to regenerate the first saline solution.

14. The method of claim 7 , wherein the regeneration process comprises applying the process of electrodialysis comprising:

i) providing a spent dilute solution formed from the first saline solution, wherein the spent dilute solution contains salt;

ii) providing a spent concentrated solution formed from the second saline solution; and

iii) supplying electricity to separate the salt into ions and move ions from the spent dilute solution to the spent concentrated solution;

wherein salinity of the spent dilute solution decreases to regenerate the first saline solution while salinity of the spent concentrated solution increases to regenerate the second saline solution.

15. The method of claim 7 , wherein the regeneration process comprises applying the process of evaporation comprising:

i) providing a spent concentrated solution formed from the second saline solution;

ii) heating the spent concentrated solution to produce water vapor; and

iii) transferring the water vapor to mix with a spent dilute solution;

wherein salinity of the spent dilute solution decreases to regenerate the first saline solution while salinity of the spent concentrated solution increases to regenerate the second saline solution.

16. The method of claim 7 , wherein the regeneration process comprises applying the process of membrane distillation comprising:

i) providing a membrane distillation vessel comprising a hydrophobic membrane having a spent concentrate solution on one side of the hydrophobic membrane and a spent dilute solution on an opposite side of the hydrophobic membrane; and

ii) warming the spent concentrate solution to produce water vapor;

wherein the water vapor permeates the hydrophobic membrane to mix with the spent dilute solution to regenerate the first saline solution while salinity of the spent concentrated solution increases to regenerate the second saline solution.

17. The method of claim 7 , wherein the regeneration process comprises applying the process of forward osmosis comprising:

circulating a spent concentrated solution and draw solution through a forward osmosis system to regenerate the second saline solution and produce a spent draw solution; and

circulating the spent draw solution through a switchable solubility system to regenerate the draw solution and to produce water.

18. The method of claim 17 , wherein the process of forward osmosis further comprises mixing the water with a spent dilute solution to regenerate the first saline solution.

Continuity (4)

References Cited (400)