Granted Patent B2

US 12,304,850 · App. 18/771,104 · Granted May 20, 2025

Inventors: Andrew Thomas Healy (Minneapolis, MN); Evan Anthony Leslie (Minneapolis, MN); Zekun Liu (Brooklyn Park, MN); Terrance P. Smith (Woodbury, MN); Joseph Reuel Levine Tirado (Minneapolis, MN)

Assignee: Claros Technologies Inc.

C02F9/00B01J41/00C02F1/32C02F1/42C02F1/441C02F1/442C02F1/46109C02F1/469C02F1/722C02F5/06C02F1/02C02F1/325C02F2001/425C02F2001/46133C02F2001/46152C02F1/4676C02F1/66C02F1/70C02F1/78C02F2101/12C02F2101/163C02F2101/36C02F2103/06C02F2201/322C02F2201/3225C02F2201/3227C02F2201/46115C02F2201/4616C02F2201/4619C02F2305/02

Abstract

Claims (35)

1. A method of PFAS destruction comprising:

a. adding an amount of persulfate and acid or base to an aqueous solution including PFAS to decrease or increase a pH and subjecting the aqueous solution including PFAS to an increased temperature and pressure of at least about 1 bar for a period of time sufficient for thermal oxidation;

b. after step a, adding a sulfite salt to the aqueous solution including PFAS;

c. after step a, if the pH of the aqueous solution is less than about 10, adding base to the aqueous solution including PFAS to increase the pH to about 10 or more; and

d. after steps a-c, irradiating the aqueous solution including PFAS with light at 222 nm.

2. The method of claim 1 wherein adding acid or base in step a comprises adding base to the aqueous solution including PFAS in an amount sufficient to raise the pH of the aqueous solution including PFAS to about 10 or more.

3. The method of claim 2 further comprising, after step a and before step d, adding a halide salt to the aqueous solution including PFAS.

4. The method of claim 3 wherein the halide salt is a bromide salt.

5. The method of claim 3 wherein the halide salt is an iodide salt.

6. The method of claim 3 further comprising adding a carbonate salt to the aqueous solution including PFAS.

7. The method of claim 1 wherein irradiating the aqueous solution including PFAS destroys greater than about 90% of the PFAS in the solution.

8. The method of claim 1 wherein irradiating the aqueous solution including PFAS in step d destroys greater than about 99% of the PFAS in the solution.

9. The method of claim 1 wherein the increased temperature comprises about 100 to about 140 degrees Celsius and the increased pressure comprises about 1 to about 5 bar.

10. A photoreactor for PFAS destruction comprising:

a reactor vessel configured to receive an aqueous solution including PFAS;

a first light source comprising an ultraviolet light source configured to deliver light at about 222 nm to the aqueous solution including PFAS in the reactor vessel;

a second light source comprising an ultraviolet light source configured to deliver light at about 222 nm to the aqueous solution including PFAS in the reactor vessel.

11. The photoreactor of claim 10 wherein the first and second light sources comprise krypton/chloride excimer lamps.

12. The photoreactor of claim 10 wherein the photoreactor is a continuous reactor configured to continuously flow the aqueous solution including PFAS through the photoreactor.

13. The photoreactor of claim 12 wherein the reactor vessel comprises a stirred tank reactor vessel.

14. The photoreactor of claim 10 further comprising a tank of a sulfite salt configured to deliver the sulfite salt to the aqueous solution upstream of or within the reactor vessel.

15. The photoreactor of claim 14 further comprising a tank of halide salt configured to deliver halide salt to the aqueous solution upstream of or within the reactor vessel.

16. The photoreactor of claim 15 further comprising a source of base configured to deliver base to the aqueous solution upstream of or within the reactor vessel such that the aqueous solution has a pH of about 10 or more within the reactor vessel.

17. The method of claim 1 further comprising, separately from step a and before steps b-d, adding an additional amount of persulfate to the aqueous solution including PFAS and subjecting the aqueous solution including PFAS to an increased temperature and pressure for a period of time sufficient for thermal oxidation.

18. The photoreactor for PFAS destruction of claim 10 further comprising:

additional light sources comprising ultraviolet light source configured to deliver light at about 222 nm to the aqueous solution including PFAS in the reactor vessel.

19. A system of PFAS destruction comprising:

a pretreatment reactor comprising:

a pre-treatment vessel configured to contain an aqueous solution containing PFAS at elevated pressure and comprising a heating element to heat the aqueous solution contained therein; and

sources of persulfate and acid or base configured to deliver persulfate and acid or base to the aqueous solution before or within the pre-treatment vessel;

a photoreactor downstream of the pretreatment reactor, the photoreactor comprising:

a reactor vessel configured to receive an aqueous solution;

a plurality of ultraviolet light sources configured to deliver light at 222 nm to the aqueous solution including PFAS in the reactor vessel; and

a source of a sulfite salt configured to deliver the sulfite salt to the aqueous solution before or within the reactor vessel.

20. The system of claim 19 further comprising a source of halide salt configured to deliver the halide salt to the aqueous solution before or within the reactor vessel.

Assignments (1)

Continuity (4)

References Cited (400)