Direct answer
Does pyrolysis destroy PFAS?
It cleans the solid. It does not automatically destroy the fluorine. Nature Reviews Clean Technology (2026): removal efficiencies can exceed 90% above 700 °C, but mineralisation is generally <40% below 700 °C and PIDs (including perfluorocarbon greenhouse gases and short PFCAs such as TFA) form. Complete mineralisation is rarely claimed below ~950 °C without additives.
Numbers from solids
| System | T | What was measured | Result |
|---|---|---|---|
| PFAS-spiked sand, lab | ≥400 °C | Σ24 PFAS in solid | ≥99.6% removal; <LOQ at 500–700 °C (Hušek 2024) |
| Sewage sludge, lab | 400 °C | Σ18 PFAS solid | 99.9% removal vs feed; gas/condensate still loaded |
| Sewage sludge, lab | ≥500 °C | Σ18 PFAS solid | 100% of the list <LOQ in char |
| Biosolids continuous bench | 500 °C | Mass through char/oil/gas | ~97–100% off char; ~84% “destroyed” system-wide; rest in gas |
| Biosolids continuous bench | 700 °C | Mass through all phases | ~95–96% system reduction; char non-detect |
| Diverse organic wastes | 500–800 °C | RE corrected for yield | >96.9% off char; <2% of PFAStot stays in char |
| PYREG / Bioforcetech (EPA ORD) | ~600 °C solids, 10 min + gas 850 °C | Sludge solids | Complete removal from solids in that test design |
| Fårevejle WWTP | 650 °C, >3 min | 7 PFAS in feed | None detected after pyrolysis (vendor/case report) |
| Kleve WWTP case pack | PYREG train | 50 PFAS | All <LQ in biochar and ash; total F slightly concentrates |
Gas-phase kinetics (why 500 °C is not enough)
- Parent PFAA headgroups come off at gas-phase T ≲ 700 °C (HF elimination or homolysis, headgroup-dependent).
- The bottleneck to mineralisation is often 1H-perfluoroalkanes, needing up to ~950 °C at 2 s (ACS ES&T Eng. 2025).
- PFOA pyrolysis model (ncsuPFASmech, 2026): <680 °C α-lactone / HF path; >680 °C chain scission. Near-complete parent loss in milliseconds needs ≥800 °C — and still needs H2, H2O or hydrocarbons to make HF rather than CF4.
- EPA Rainbow Furnace: incomplete PFOA incineration regenerates smaller PFCAs, including TFA.
- Science Advances 2025: PFHxA products from 700 °C; radicals and CF2 species at 950 °C.
Additives that lower the mineralisation temperature
Nature Reviews 2026: activated carbon can raise PFOA mineralisation ~10× at ≤400 °C by concentrating vapours. Alkali / alkaline-earth additives convert F to CaF2 and have been reported at >95% mineralisation at 500 °C. That is a different recipe than a bare steel kiln.
TFA is a special case
Trifluoroacetic acid is short, water-soluble, and both a pollutant and a PID. Hydrothermal processing in compressed water at 150–250 °C, P < 30 MPa transforms TFA to CHF3 + CO2; NaOH then mineralises CHF3 to fluoride, formate and carbonate (ES&T 2024). Kinetics are limited by thermal decarboxylation, not by [NaOH]. Do not advertise a 500 °C sludge kiln as a TFA water-treatment plant.
How to manage PFAS pyrolysis
- Dry feed (PFAS ride with water vapour too).
- Solids ≥500–600 °C if the KPI is non-detect char (sludge).
- Contain vapour. No fugitive hatches.
- Oxidise pyrolysis gas ≥850–950 °C with steam or fuel-H, then quench fast (dioxin window if Cl is present).
- Scrub HF; consider Ca/alkali in-bed if mineralisation in-kiln is the design.
- Measure: targeted PFAS + TOP + TOF/EOF + stack PIDs — not char-only.