Salt Separation and Destruction of PFAS Utilizing Reverse Osmosis and Salt Separation

Patent metadata

Field	Value
Publication number	US-2022041483-A1
Application number	US-202117396599-A
Country	US
Kind code	A1
Filing date	Aug 6, 2021
Priority date	Aug 6, 2020
Publication date	Feb 10, 2022
Grant date	—

Abstract

Per- and polyfluoroalkyl substances (PFAS) are destroyed by oxidation in supercritical conditions. PFAS in water is concentrated in a reverse osmosis step and salt from the resulting solution is removed in supercritical conditions prior to destruction of PFAS in supercritical conditions.

First claim

What is claimed:

1 . A method of destroying PFAS, comprising: providing an aqueous solution comprising water and PFAS;
subjecting the aqueous solution to reverse osmosis to produce a clean water fraction and a briny concentrated fraction in which the PFAS concentration is at least 50% greater than the aqueous solution; preheating the briny concentrated fraction in a heat exchanger to form a preheated concentrated fraction that is at subcritical conditions; passing the preheated concentrated fraction into a heated pre-reactor where the briny concentrated fraction is converted to supercritical conditions at a first temperature causing sodium chloride to precipitate; removing at least a portion of the sodium chloride to produce a brine-reduced fraction; passing the brine-reduced fraction to a reactor where the fraction is subjected to oxidation under supercritical conditions wherein the concentration of oxidant and/or temperature is higher than in the pre-reactor; producing a clean hot water solution having a concentration of PFAS that is at least 90% less than the aqueous solution; and, optionally, transferring heat from the clean hot water solution to the aqueous solution in the heat exchanger in the preheating step.

2 . The method of claim 1 wherein the aqueous solution is filtered prior to reverse osmosis.

3 . The method of claim 1 wherein the effluent passes through a post heat exchanger that is positioned downstream of the pre-reactor and then passes through a pre heat exchanger that is positioned upstream of the pre-reactor.

4 . The method of claim 1 wherein the aqueous solution comprising water and PFAS has a first volume;
wherein 10% or less of the first volume is subjected to supercritical conditions; and
wherein, in said method, at least 95% of the PFAS in the first volume is destroyed in supercritical conditions.

5 . The method of claim 1 wherein the briny concentrated fraction in which the PFAS concentration is at least 50% greater, that results from the reverse osmosis and prior to the step of removing at least a portion of the sodium chloride, comprises a precipitate and further comprising a step of adding an acid to dissolve the precipitate.

6 . The method of claim 1 wherein the pre-reactor comprises a first tube leading into a collector vessel and a second tube passing out of the collector vessel, wherein the collector vessel comprises an inner diameter that is at least twice as large as the inner diameter of the first tube;
and, optionally, wherein a fuel or oxidizer is added to the pre-reactor.

7 . The method of claim 1 wherein the pre-reactor comprises a transcritical hydrocyclone, comprising:
a conical chamber comprising: an inlet for introducing supercritical fluid into the conical chamber tangentially along an inner wall of the cyclone;
a top outlet adapted for flow of a supercritical fluid;
an exit pipe adapted for flow of a liquid;

a cone disposed in the conical chamber adapted such that a channel can be formed between the inner wall of the cyclone and an outer wall of the cone; and
wherein the cone comprises a bottom opening.

8 . A system for destroying PFAS, comprising:
a reverse osmosis system; a conduit from the reverse osmosis system to a salt separator; wherein the salt separator comprises a first tube leading into a collector vessel and a second tube passing out of the collector vessel, wherein the collector vessel comprises an inner diameter that is at least twice as large as the inner diameter of the first tube; and a conduit from the salt separator to a supercritical reactor.

9 . The system of claim 8 wherein the collector vessel comprises a supercritical fluid.

10 . The system of claim 8 wherein the first tube projects at least 5 cm into the collector vessel and the second tube does not project into the interior of the collector tube.

11 . The system of claim 8 further comprising a first heat exchanger disposed in the conduit between the reverse osmosis system and the salt separator;
wherein, during operation, the first heat exchanger exchanges heat between a subcritical PFAS-containing aqueous stream and a return stream of PFAS-free water from the supercritical reactor.

12 . The system of claim 8 wherein the first tube projects at least 5 cm further into the collector vessel than the second tube.

13 . The system of claim 11 wherein the heat exchanger is a tube-in-tube heat exchanger.

14 . The system of claim 11 wherein the salt separator comprises a plurality of collector vessels each collector vessel comprising a set of an inlet tube and an outlet tube; wherein each set is at a higher temperature that the previous set in the direction of flow.

15 . A transcritical hydrocyclone, comprising:
a conical chamber comprising: an inlet for introducing supercritical fluid into the conical chamber tangentially along an inner wall of the cyclone;
a top outlet adapted for flow of a supercritical fluid;
an exit pipe adapted for flow of a liquid;
a cone disposed in the conical chamber adapted such that a channel can be formed between the inner wall of the cyclone and an outer wall of the cone; and
wherein the cone comprises a bottom opening.

16 . The transcritical hydrocyclone of claim 15 wherein the bottom opening comprises a diffuser; wherein the diffuser comprises a plurality of openings.

17 . The transcritical hydrocyclone of claim 15 wherein the plurality of openings comprise an open area that is at least two times or at least three times as large as the cross-sectional area of the exit pipe.

18 . The transcritical hydrocyclone of claim 15 wherein the openings are angled from the central axis to an inner wall of the lower pipe.

19 . The transcritical hydrocyclone of claim 15 further comprising a mechanism adapted to move the cone along the central axis of the conical chamber relative to the inner wall of the conical chamber.

20 . The transcritical hydrocyclone of claim 15 comprising heat exchanger thermally connected to an outer wall of the conical chamber.

21 . The transcritical hydrocyclone of claim 20 wherein the heat exchanger comprises a jacket for fluid flow.

22 . The method of claim 1 wherein the pre-reactor and/or the reactor comprise reactor walls coated with a ceramic coating that is resistant to hydrofluoric acid.

23 . The method of claim 22 wherein the ceramic comprises: B4C (boron carbide), SiC (silicon carbide), TaC (tantalum carbide), WC (tungsten carbide), metal fluorides such as YF3 (yttrium fluoride), YN (yttrium nitride), LaF3 (lanthanum fluoride), LaN (lanthanum nitride), YbN, YbF3, or any lanthanide nitride or lanthanide fluoride, HfN (hafnium nitride), CeN (cerium nitride), CeF3 (cerium fluoride), TaN (tantalum nitride), Ta (tantalum), TaF (tantalum fluoride), ZrN (zirconium nitride), ZrF (zirconium fluoride), WN (tungsten nitride), or combinations thereof.

24 . The method of claim 22 wherein the ceramic comprises at least 80 wt % chromium oxide.

Assignees

• Battelle Memorial Institute

Inventors

• Rosansky Stephen H
• Miller Michael
• Norris Patrick
• Argumedo Darwin
• Hendry Douglas
• Haggerty Ian
• Brown Keith
• James Joshua
• Casciano Joe
• Winecki Slawomir
• Lal Vivek
• Mcguinness Tom

Classifications

• B01D2313/221

  Heat exchangers · CPC title

• B01D21/267

  by using a cyclone · CPC title

• B01D61/08

  Apparatus therefor · CPC title

• B01D2311/1031

  Heat integration, heat recovery or reuse within an apparatus · CPC title

• Y02W10/30

  Wastewater or sewage treatment systems using renewable energies · CPC title