Granted Patent B2

US 12,195,364 · App. 17/666,870 · Granted Jan 14, 2025

Inventors: Steven E. Woodard (Cumberland, ME); John C. Berry (Mooresville, NC); Michael G. Nickelsen (Fuquay-Varina, NC)

Assignee: Emerging Compounds Treatment Technologies, Inc.

C02F1/42B01J41/05B01J49/07C02F2001/422C02F2101/36C02F2301/08C02F2303/16

Abstract

Claims (21)

1. A system for removing long-chain and short-chain per- and polyfluoroalkyl substances (PFAS) from contaminated water using at least two different regenerable anion exchange resins, the system comprising:

at least one first anion exchange resin vessel configured to receive a flow of water contaminated with long and short-chain PFAS compounds, the at least one first anion exchange resin vessel including a first regenerable anion exchange resin therein having a high affinity for long-chain PFAS compounds configured such that a majority of the long-chain PFAS compounds sorb to the first regenerable anion exchange resin to remove the majority of the long-chain PFAS compounds from the flow of the contaminated water and produce a flow of water having a majority of the long-chain PFAS compounds removed;

at least one second anion exchange resin vessel, the second anion exchange resin vessel configured to receive the flow of water having the majority of the long-chain PFAS compounds removed, the at least one second anion exchange resin vessel including a second regenerable anion exchange resin therein having a high affinity for short-chain PFAS compounds and configured such that a majority of the short-chain PFAS compounds sorb to the second anion exchange resin to remove the majority of the short-chain PFAS compounds from the contaminated water and produce a treated flow of water having a majority of the long and short-chain PFAS compounds removed, and

wherein the second regenerable anion exchange resin includes a macroporous resin including functional groups configured to increase the affinity of the short-chain PFAS compounds to the second regenerable anion exchange resin and increase a capacity of the second regenerable anion exchange resin to remove the short-chain PFAS compounds from the flow of water having the majority of the long-chain PFAS compounds removed; and

wherein selecting to increase length and basicity of the functional groups increases the affinity of the short-chain PFAS compounds to the second regenerable anion exchange resin.

2. The system of claim 1 including a resin regeneration subsystem configured to introduce a flow of a solution into the at least one second regenerable anion exchange resin vessel to regenerate the second regenerable anion exchange resin and produce a flow of a first spent regenerant solution.

3. The system of claim 2 in which the resin regeneration subsystem includes introducing the flow of the first spent regenerant solution or another flow of regenerant solution into the at least one first anion exchange resin vessel to regenerate the first regenerable anion exchange resin and produce a flow of a second spent regenerant solution.

4. The system of claim 1 in which the first regenerable anion exchange resin and the second regenerable anion exchange resin include a macroporous, strong base, anion exchange resin.

5. The system of claim 1 in which the at least one first anion exchange resin vessel includes at least one lead vessel and at least one lag vessel.

6. The system of claim 1 in which the at least one second anion exchange resin vessel includes at least one lead vessel and at least one lag vessel.

7. A system for removing long-chain and short-chain per- and polyfluoroalkyl substances (PFAS) from contaminated water using at least two different regenerable anion exchange resins, the system comprising:

at least one anion exchange resin vessel configured to receive a flow of water contaminated with long and short-chain PFAS compounds, the at least one anion exchange resin vessel including a first regenerable anion exchange resin therein having a high affinity for long-chain PFAS compounds configured such that a majority of the long-chain PFAS compounds sorb to the first regenerable anion exchange resin to remove the majority of the long-chain PFAS compounds from the contaminated water and produce a flow of water having a majority of the long-chain PFAS compounds removed;

the at least one anion exchange resin vessel further including a second regenerable anion exchange resin therein, the second regenerable resin configured to receive the flow of water having the majority of the long-chain PFAS compounds removed, the second regenerable anion exchange resin having a high affinity for short-chain PFAS compounds and configured such that a majority of the short-chain PFAS compounds sorb to the second regenerable anion exchange resin to remove the majority of the short-chain PFAS compounds from the contaminated water and produce a treated flow of water having a majority of the long and short-chain PFAS compounds removed;

wherein the second regenerable anion exchange resin includes a macroporous resin including functional groups configured to increase the affinity of the short-chain PFAS compounds to the second regenerable anion exchange resin and increase a capacity of the second regenerable anion exchange resin to remove the short-chain PFAS compounds from the flow of water having the majority of the long-chain PFAS compounds removed; and

wherein selecting to increase length and basicity of the functional groups increases the affinity of the short-chain PFAS compounds to the second regenerable anion exchange resin.

8. The system of claim 7 in which the at least one anion exchange resin vessel includes at least one lead vessel train and at least one lag vessel train.

9. The system of claim 7 including a resin regeneration subsystem configured to introduce a flow of a regenerant solution into the second regenerable anion exchange resin to regenerate the second regenerable anion exchange resin and produce a flow of a first spent regenerant solution.

10. The system of claim 9 in which the resin regeneration subsystem includes introducing the flow of the first spent regenerant solution or another flow of regenerant solution into the first regenerable anion exchange resin to regenerate the first regenerable anion exchange resin and produce a flow of a second spent regenerant solution.

11. The system of claim 7 in which the first regenerable anion exchange resin and the second regenerable anion exchange resin include a macroporous, strong base, anion exchange resin.

12. The system of claim 8 in which the at least one lead vessel train includes a plurality of anion exchange resin vessels connected in series such that one of the plurality of anion exchange resin vessel is configured to receive the flow of contaminated water and includes the first regenerable anion exchange resin therein to remove the majority of the long-chain PFAS compounds from the contaminated water and produce the flow of water having the majority of the long-chain PFAS compounds removed and another of the plurality of anion exchange resin vessels is configured to receive the flow of contaminated water having a majority of the long-chain PFAS compounds removed and including the second regenerable anion exchange resin therein to remove the majority of the short-chain PFAS compounds and produce the treated flow of water having the majority of the long and short-chain PFAS compounds removed.

13. The system of claim 8 in which the at least one lag vessel train includes a plurality of anion exchange resin vessels connected in series configured to receive the treated flow of water which may have carryover short-chain PFAS compounds therein and output the treated flow of water having the majority of the long and short-chain PFAS compounds removed.

Assignments (5)

Continuity (2)

References Cited (17)