IP Library › Granted Patent US 12,599,800
Granted Patent B2
US 12,599,800 · App. 18/064,025 · Granted Apr 14, 2026

Processes for removing perfluoroalkyl substances and regenerating an adsorbent used with same

Inventors: Amanda J. Hickman (Evanston, IL); Erin M. Broderick (Arlington Heights, IL); Susan C. Koster (Carpentersville, IL); Benjamin D. Yuhas (Evanston, IL); Aric G. Fisher (Tulsa, OK); William J. Whyman (Collinsville, OK); Gregory B. Kuzmanich (Arlington Heights, IL)
Assignee: UOP LLC
A62D3/36B01D15/203B01J20/16B01J20/20B01J20/3416B01J20/345B01J20/3483B01J49/40B01J49/50C02F1/281C02F1/283C02F1/42A62D2101/22C02F2101/36C02F2303/16
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Quick Facts
Patent No.
US 12,599,800
App. No.
18/064,025
Granted
Apr 14, 2026
Kind
B2
Abstract

Processes and apparatuses for degrading PFAS into calcium fluoride, carbon dioxide, and water. PFAS are heated and introduced to a calcium base which will degrade the PFAS. The PFAS may be in a stream that is a PFAS enriched stream formed by desorbing the PFAS from an adsorbent which removed the PFAS from a contaminant stream. The PFAS may be desorbed in the presence of the calcium base. The calcium base may be calcium hydroxide, calcium oxide, calcium carbonate, or combinations thereof.

Claims (14)

1 . A process for degradation of PFAS, the process comprising:

heating PFAS to provide a heated PFAS stream; and,

introducing the heated PFAS stream to a vessel containing a calcium base so as to convert the PFAS into calcium fluoride, carbon dioxide, and water,

wherein a molar ratio of calcium to fluoride in the vessel is between 1.0 to 10.

2 . The process of claim 1 , wherein the PFAS have a temperature between 400° C. to 925° C. when the heated PFAS stream is introduced into the vessel.

3 . The process of claim 2 , wherein the temperature is between 525° C. to 825° C.

4 . The process of claim 1 , wherein the calcium base comprises calcium hydroxide, calcium oxide, calcium carbonate, or combinations thereof.

5 . The process of claim 1 , wherein the calcium base consists of calcium oxide.

6 . The process of claim 1 , wherein the heated PFAS stream is introduced to the vessel for a time between 0.5 seconds to 10 minutes.

7 . The process of claim 1 , further comprising:

separating the calcium fluoride, carbon dioxide, and water into a stream comprising carbon dioxide and water and the solid calcium fluoride.

8 . The process of claim 7 , further comprising:

removing the carbon dioxide in a carbon dioxide scrubber.

9 . The process of claim 1 , wherein the PFAS is heated in the absence of the calcium base to a temperature between 400° C. to 925° C.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 9, 2023
From: HICKMAN, AMANDA J.; BRODERICK, ERIN M.; KOSTER, SUSAN C.; YUHAS, BENJAMIN D.; KUZMANICH, GREGORY B.; FISHER, ARIC G.; WHYMAN, WILLIAM J.
To: UOP LLC
Reel/Frame 062316/0559 →
Continuity (1)
Related Publication 20240189644A1 · Jun 13, 2024
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