Methods and systems for electrochemical oxidation of polyfluoroalkyl and perfluroalkyl contaminants
The present disclosure provides methods, electrodes, and systems for electrochemical oxidation of polyfluoroalkyl and perfluroalkyl (PFAS) contaminants using Magnéli phase titanium suboxide ceramic electrodes/membranes. Magneli phase titanium suboxide ceramic electrodes/membranes can be porous and can be included in reactive electrochemical membrane filtration systems for filtration, concentration, and oxidation of PFASs and other contaminants.
1. A method for electrochemically oxidizing polyfluoroalkyl and perfluoroalkyl substances (PFASs), the method comprising:
contacting an aqueous composition contaminated with one or more types of PFASs with a Magnéli phase titanium oxide ceramic electrode comprising one or more Magnéli phase titanium sub-oxides wherein at least one of the Magnéli phase titanium sub-oxides is Ti 4 O 7 or Ti 5 O 9 ; and
supplying electric current to the Magnéli phase titanium oxide ceramic electrode in an electrochemical cell, whereby the electrode electrochemically oxidizes the PFASs to oxidatively degrade the PFASs into mineral components, inorganic components, or both, wherein the one or more types of PFASs comprise at least one type of perfluoroalkyl acid (PFAA).
2. The method of claim 1 , wherein the Magnéli phase titanium oxide ceramic electrode comprises T 4 O 7 or a combination of Ti 4 O 7 and Ti 5 O 9 .
3. The method of claim 1 , wherein the composition contaminated with PFASs comprises wastewater and the method further comprises pre-treating the wastewater to concentrate the PFASs prior to contact with the Magnéli phase titanium oxide ceramic electrode.
4. The method of claim 3 , wherein the wastewater is pre-treated via electrocoagulation to concentrate the PFASs.
5. The method of claim 2 , wherein the Magnéli phase titanium oxide ceramic electrode comprises a plurality of micropores.
6. The method of claim 5 , wherein the plurality of micropores have a diameter from about 10 nm to 10 μm.
7. The method of claim 5 , wherein the Magnéli phase titanium oxide ceramic electrode has a porosity of about 5-75%.
8. The method of claim 1 , wherein the at least one type of PFAA is selected from: perfluorooctanoate (PFOA), perfluorooctanesulfonate (PFOS) or a combination thereof.
9. The method of claim 1 , wherein the composition contaminated with PFASs comprises contaminated wastewater, and the method further comprises:
producing at least partially decontaminated wastewater after contact with the Magnéli phase titanium oxide ceramic electrode electrochemically oxidizes the PFASs.
10. The method of claim 9 , further comprising recycling the at least partially decontaminated wastewater.
11. The method of claim 1 , wherein the Magnéli phase titanium oxide ceramic electrode comprises a plurality of pores and serves as both an anode and a membrane in a reactive electrochemical membrane (REM) filtration system.
12. The method of claim 1 , wherein the at least one type of PFAA is selected from: a perfluoroalkyl carboxylic acid (PFCA), a perfluoroalkyl sulfuric acid (PFSA), or a combination thereof.
13. The method of claim 1 , wherein the at least one type of PFAA comprises at least one perfluoroalkyl sulfuric acid (PFSA).
14. A method for electrochemically oxidizing polyfluoroalkyl and perfluoroalkyl substances (PFASs), the method comprising:
contacting an aqueous composition contaminated with one or more types of PFASs with an electrochemical cell comprising a first Magnéli phase titanium oxide ceramic membrane electrode configured to serve as an anode and a second Magnéli phase titanium oxide ceramic membrane electrode configured to serve as a cathode, wherein the first and second Magnéli phase titanium oxide ceramic membrane electrodes each comprise one or more Magnéli phase titanium sub-oxides wherein at least one of the Magnéli phase titanium sub-oxides is Ti 4 O 7 or Ti 5 O 9 ; and
supplying electric current to the electrochemical cell such that the first Magnéli phase titanium oxide ceramic membrane electrode electrochemically oxidizes the PFASs to oxidatively degrade the PFASs into mineral components, inorganic components, or both, and the second Magnéli phase titanium oxide ceramic membrane electrode serves as the cathode.
15. The method of claim 14 , wherein the cathode reduces chlorate to Cl − .
16. A method for electrochemically oxidizing polyfluoroalkyl and perfluoroalkyl substances (PFASs), the method comprising:
contacting an aqueous composition contaminated with one or more types of PFASs and trichloroethylene (TCE) with an electrochemical cell comprising a first Magnéli phase titanium oxide ceramic electrode configured to serve as an anode and a second Magnéli phase titanium oxide ceramic membrane electrode configured to serve as a cathode, wherein the first and second Magnéli phase titanium oxide ceramic membrane electrodes each comprise one or more Magnéli phase titanium sub-oxides wherein at least one of the Magnéli phase titanium sub-oxides is Ti 4 O 7 or Ti 5 O 9 and wherein each electrode has at least a portion of the electrode coated with activated carbon fiber (ACF); and
supplying electric current to the electrochemical cell such that the first Magnéli phase titanium oxide ceramic membrane electrode electrochemically oxidizes the PFASs to oxidatively degrade the PFASs into mineral components, inorganic components, or both, and the second Magnéli phase titanium oxide ceramic membrane electrode serves as the cathode and reduces chlorate to Cl − .
17. The method of claim 16 , wherein the first and second Magnéli phase titanium oxide ceramic electrodes have a tubular shape.