Sustainable system and method for removing and concentrating per- and polyfluoroalkyl substances (PFAS) from water
A sustainable system for removing and concentrating per- and polyfluoroalkyl substances (PFAS) from water. The system includes an anion exchange vessel having a selected anion exchange resin therein configured to remove PFAS from the water. A line coupled to the vessel introduces a flow of water contaminated with PFAS such that the PFAS bind to the selected anion exchange resin and are thereby removed from the water. A regenerant solution line is coupled to the anion exchange vessel to introduce an optimized regenerant solution to the anion exchange vessel to remove the PFAS from the anion exchange resin, thereby regenerating the anion exchange resin and generating a spent regenerant solution comprised of the removed PFAS and the optimized regenerant solution. A separation and recovery subsystem recovers the optimized regenerant solution for reuse and separates and concentrates the removed PFAS.
1. A system for concentrating per- and polyfluoroalkyl substances (PEAS), the system comprising:
regenerant solution line coupled to a vessel configured to introduce a regenerant solution to the vessel to remove PEAS from anion exchange resin within the vessel thereby regenerating the anion exchange resin and generating a spent regenerant solution comprising the removed PEAS and the regenerant solution; and
a separation and recovery subsystem configured to separate and concentrate PEAS to produce a concentrated PEAS solution; and;
a super-loading recovery subsystem configured to receive the concentrated PFAS solution and separate and further concentrate the removed PEAS by adsorbing the concentrated PEAS onto an adsorptive media to produce a PEAS waste product and a solution substantially without PEAS.
2. The system of claim 1 in which the regenerant solution includes a salt, a solvent, and water.
3. The system of claim 2 in which the solvent includes an alcohol.
4. The system of claim 2 , in which the super-loading recovery subsystem in addition to producing the PFAS waste product, produces a solution of concentrate salt and water capable of reuse.
5. The system of claim 1 in which the regenerant solution includes a base, a solvent, and water.
6. The system of claim 5 in which the solvent includes an alcohol.
7. The system of claim 5 in which the super-loading recovery subsystem in addition to producing the PFAS waste product, produces a solution of concentrated base solution and water capable of reuse.
8. The system of claim 7 in which the super-loading recovery subsystem includes an anionic exchange resin housed in another vessel as the adsorptive media.
9. The system of claim 1 in which the regenerant solution includes a base and a solvent.
10. The system of claim 9 in which the solvent includes an alcohol.
11. The system of claim 9 in which the super-loading recovery subsystem in addition to producing the PFAS waste product, produces a solution of concentrated base capable of reuse.
12. The system of claim 11 in which the super-loading recovery subsystem includes an anionic exchange resin housed in another vessel as the adsorptive media.
13. The system of claim 1 in which the regenerant solution includes a salt and a solvent.
14. The system of claim 13 in which the solvent includes an alcohol.
15. The system of claim 13 in which the super-loading recovery subsystem in addition to producing the PFAS waste product, produces a solution of concentrate salt capable of reuse.
16. The system of claim 15 in which the super-loading recovery subsystem includes an anionic exchange resin as the adsorptive media housed in another vessel as the adsorptive media.
17. The system of claim 1 in which the anion exchange resin includes a macroporous, strong base, anion exchange resin.
18. The system of claim 1 in which the separation and recovery subsystem includes one or more of: an evaporation subsystem, a distillation subsystem and/or a membrane separation subsystem.
19. The system of claim 1 in which the separation and recovery subsystem includes a solvent purification subsystem configured to remove carryover PFAS from the separation and to provide a purified, reclaimed solvent capable of reuse.
20. The system of claim 19 in which the solvent purification subsystem includes an additional vessel including an anion exchange resin therein.
21. The system of claim 1 in which the super-loading recovery subsystem includes an anionic exchange resin as the adsorptive media housed in another vessel.
22. A method for concentrating per- and polyfluoroalkyl substances (PFAS), the method comprising:
introducing a regenerant solution to anion exchange resin to remove PFAS from the anion exchange resin thereby regenerating the anion exchange resin and generating a spent regenerant solution comprising removed PFAS and the regenerant solution;
separating and concentrating the removed PEAS to produce a concentrated PFAS solution;
subjecting the concentrated PEAS solution to a super-loading recovery process to separate and further concentrate the removed PFAS by adsorbing concentrated PFAS onto an adsorptive media to produce a PFAS waste product and a solution substantially without PFAS.
23. The method of claim 22 in which the regenerant solution includes a salt, a solvent, and water.
24. The system of claim 23 in which the solvent includes an alcohol.
25. The method of claim 22 in which the regenerant solution includes a base, a solvent, and water.
26. The system of claim 25 in which the solvent includes an alcohol.
27. The method of claim 22 in which the regenerant solution includes a base and a solvent.
28. The system of claim 27 in which the solvent includes an alcohol.
29. The method of claim 22 in which the regenerant solution includes a salt and a solvent.
30. The system of claim 29 in which the solvent includes an alcohol.
31. The method of claim 22 in which the anion exchange resin includes a macro-porous, strong base, anion exchange resin.
32. The method of claim 22 in which the separating and concentrating includes one or more of evaporation, distillation and/or membrane separation.
33. The method of claim 22 in which the separating and concentrating includes removing carryover PFAS and providing a purified reclaimed solvent capable of reuse.