IP Library Granted Patent US 11,365,133
Granted Patent B1
US 11,365,133 · App. 16/400,522 · Granted Jun 21, 2022

Vacuum freezing nucleated liquid water for purifying brackish water

Inventors: Fangyu Cao (Alexandria, VA); Jianjian Wang (Lancaster, PA); Howard Pearlman (Haddon Township, NJ)
Assignee: ADVANCED COOLING TECHNOLOGIES, INC.
C02F1/22C02F1/265C02F2103/08
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Quick Facts
Patent No.
US 11,365,133
App. No.
16/400,522
Filed
May 1, 2019
Granted
Jun 21, 2022
Kind
B1
Art Unit
3763
USPC
62/100
Abstract

A method of purifying brackish water includes mixing brackish water with a nucleating agent, forming nucleated liquid water and distributing droplets of the nucleated liquid water inside a vacuum chamber, vacuum freezing the droplets of the nucleated liquid water in the vacuum chamber. The method further includes the droplets forming pure water vapor, nucleated ice, and remaining brackish water, mixing and liquifying the pure water vapor and the nucleated ice, forming a mixture of purified liquid water and the nucleating agent. The method further includes separating the mixture of purified liquid water and the nucleating agent, forming purified liquid water and the nucleating agent.

Claims (37)

1. A method of purifying brackish water comprising:

mixing brackish water with a nucleating agent, forming nucleated liquid water;

distributing droplets of the nucleated liquid water inside a vacuum chamber;

vacuum freezing the droplets of the nucleated liquid water in the vacuum chamber, the droplets forming pure water vapor, nucleated ice, and remaining brackish water;

mixing and liquifying the pure water vapor and the nucleated ice, forming a mixture of purified liquid water and the nucleating agent; and

separating the mixture of purified liquid water and the nucleating agent, forming purified liquid water and the nucleating agent.

2. The method of claim 1 , wherein the nucleating agent is taken from the group consisting of AgI, CuI, AgCl, Ag x Cu 1-x I, and combination thereof.

3. The method of claim 2 , wherein particles of the nucleation agent are between 50 nanometers and 0.1 mm in diameter.

4. The method of claim 1 , wherein the droplets of the nucleated liquid water are between 20 microns and 1.5 millimeters in diameter.

5. The method of claim 1 , wherein vacuum freezing occurs at or below a temperature and pressure corresponding to a triple point of water.

6. The method of claim 5 , wherein during vacuum freezing, subcooling of the remaining brackish water in the vacuum chamber is maintained at 2 degrees C. or less.

7. The method of claim 5 , wherein during vacuum freezing, subcooling of the remaining brackish water in the vacuum chamber is maintained at 1 degree C. or less.

8. The method of claim 1 further comprises prior to the mixing and liquifying the pure water vapor and the nucleated ice, washing the nucleated ice with a portion of the purified liquid water to remove the brackish water from the nucleated ice.

9. The method of claim 8 further comprises pre-cooling the brackish water prior to mixing the brackish water with the nucleating agent, with remaining brackish water from the vacuum chamber.

10. The method of claim 8 further comprises, subsequent to vacuum freezing,

transporting the pure water vapor from the vacuum chamber to a regenerator by one or more of pumping, thermal ejecting, and mechanical blowing.

11. The method of claim 10 , wherein in the regenerator, at least a portion of the pure water vapor condenses on a surface of the nucleated ice,

wherein both the pure water vapor and the nucleated ice are generated in and transported from the vacuum chamber.

12. The method of claim 1 , wherein the nucleating agent is obtained by doping Cu in AgI.

13. The method of claim 12 , wherein the nucleating agent obtained by doping Cu in AgI is Ag 0.3 Cu 0.7 I.

14. The method of claim 1 , wherein during vacuum freezing, a portion of pure water of the droplets of the nucleated liquid water is frozen, while another portion of the pure water of the nucleated liquid water is vaporized, at a pressure between 200 Pa and 650 Pa.

15. The method of claim 10 further comprises a thermal ejector to pump pure water vapor from the vacuum chamber to the regenerator, the thermal ejector adapted to be driven by a thermal energy source operating at 120° C. or less.

16. The method of claim 10 further comprises a thermal ejector to pump pure water vapor from the vacuum chamber to the regenerator, the thermal ejector adapted to be driven by a thermal energy source operating at about 75° C.

17. A method of purifying brackish water comprising:

mixing brackish water with a nucleating agent, forming nucleated liquid water;

distributing droplets of the nucleated liquid water inside a vacuum chamber;

vacuum freezing the droplets of the nucleated liquid water in the vacuum chamber at or below a temperature and pressure corresponding to a triple point of water, the droplets forming pure water vapor, nucleated ice, and remaining brackish water;

mixing and liquifying the pure water vapor and the nucleated ice, forming a mixture of purified liquid water and the nucleating agent; and

separating the mixture of purified liquid water and the nucleating agent, forming purified liquid water and the nucleating agent.

18. The method of claim 17 , wherein the nucleating agent is taken from the group consisting of AgI, CuI, AgCl, Ag x Cu 1-x I, and combination thereof.

19. The method of claim 17 , wherein the nucleating agent is obtained by doping Cu in AgI.

20. The method of claim 19 , wherein the nucleating agent obtained by doping Cu in AgI is Ag 0.3 Cu 0.7 I.

21. The method of claim 17 , wherein during vacuum freezing, subcooling of the remaining brackish water in the vacuum chamber is maintained at 2 degrees C. or less.

22. The method of claim 17 further comprises, subsequent to vacuum freezing,

transporting the pure water vapor from the vacuum chamber to a regenerator by one or more of pumping, thermal ejecting, and mechanical blowing;

wherein in a regenerator, at least a portion of the pure water vapor condenses on a surface of the nucleated ice, wherein both the pure water vapor and the nucleated ice are generated in and transported from the vacuum chamber; and

a thermal ejector to pump pure water vapor from the vacuum chamber to the regenerator, the thermal ejector adapted to be driven by a thermal energy source operating at 120° C. or less.

Assignments (3)
SECURITY INTEREST Recorded May 19, 2026
From: ADVANCED COOLING TECHNOLOGIES, INC.
To: HPS INVESTMENT PARTNERS, LLC
Reel/Frame 074701/0714 →
CONFIRMATORY LICENSE Recorded Aug 22, 2025
From: ADVANCED COOLING TECHNOLOGIES, INC.
To: U.S. DEPARTMENT OF ENERGY
Reel/Frame 072532/0165 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 29, 2019
From: CAO, FANGYU; WANG, JIANJIAN; PEARLMAN, HOWARD
To: ADVANCED COOLING TECHNOLOGIES, INC.
Reel/Frame 049301/0001 →
Continuity (1)
Provisional Application 62669754 · May 10, 2018
Cited By (1)
US 12,474,070