Per- and polyfluoroalkyl substances (PFAS) have emerged as a significant challenge for water quality and public health. These persistent synthetic compounds have been linked to immune suppression, elevated cholesterol, and certain cancers, and water systems are under regulatory and public pressure to remove them. This article examines what PFAS removal efficiency actually means in practice, how it is measured, how the main technologies compare, and why a single percentage figure is rarely enough to evaluate a treatment system.
Efficiency is only one dimension of technology selection. The full comparison, including cost, footprint, and residuals, is set out in our overview of PFAS removal technologies.
Treatment claims are often stated as a single figure — “removes 90 percent” or “over 99 percent.” For PFAS, those numbers need careful interpretation:
EPA’s drinking water regulation, finalized in April 2024, set enforceable limits of 4.0 parts per trillion for PFOA and PFOS, along with limits for PFHxS, PFNA, HFPO-DA, and a hazard index for mixtures, with compliance originally due in 2029. In May 2026, EPA proposed retaining the PFOA and PFOS limits with an optional compliance extension to 2031 and rescinding the others; as of September 2026 those remain proposals. The very low concentration limits are what make efficiency — and particularly breakthrough behavior — so consequential for design and operating cost.
Coagulation, flocculation, sedimentation, and conventional filtration remove little PFAS. PFAS are dissolved, highly soluble, and not readily captured on floc, so conventional treatment trains provide minimal removal regardless of chain length. Their value in PFAS treatment is as pretreatment, reducing the organic matter and suspended solids that would otherwise shorten the life of downstream adsorptive media.
Granular activated carbon (GAC) removes PFAS by adsorption and is the most widely installed technology. Efficiency depends on:
PFAS-selective anion exchange resins generally achieve longer run times than GAC at shorter contact times and outperform GAC on many short-chain compounds, though short-chain PFAS still break through first. Resins are typically used once and then disposed of or incinerated. Competing anions such as sulfate and nitrate affect capacity.
Reverse osmosis and nanofiltration reject PFAS at very high rates — commonly above 90 percent and often above 99 percent for reverse osmosis — and their performance is relatively stable over time, unlike adsorptive media. The trade-offs are energy demand, water lost to the reject stream, and the concentrated reject itself, which contains all of the removed PFAS and must be managed.
Conventional advanced oxidation processes — ozone, UV/hydrogen peroxide, and similar hydroxyl radical systems — do not effectively degrade perfluorinated compounds such as PFOA and PFOS, and can convert some precursor compounds into regulated PFAS. They should not be counted as a PFAS removal step. Technologies that do break down PFAS, such as electrochemical oxidation and plasma, are applied to concentrated waste streams rather than full drinking water flows.
Long-chain PFAS are generally easier to remove than short-chain compounds with all adsorptive technologies. Characterizing the full PFAS profile, not just the regulated compounds, is essential, because the weakest-adsorbing compound present often governs media life.
Natural organic matter is typically the most important competing constituent for GAC, and competing anions for ion exchange. Suspended solids foul both media and membranes, and membrane scaling depends on hardness and silica.
Vessel configuration strongly affects achievable efficiency. Lead-lag arrangements allow the lead vessel to be used until breakthrough while the lag vessel protects finished water, substantially improving media utilization.
Drinking water PFAS are measured by liquid chromatography with tandem mass spectrometry (LC-MS/MS) using EPA Method 533 or 537.1. Sampling between lead and lag vessels provides early warning of breakthrough.
The most useful performance data for adsorptive systems is a breakthrough curve for each PFAS of concern, plotted as effluent concentration against bed volumes treated. These curves, developed from pilot testing or rapid small-scale column tests on the actual source water, allow media replacement frequency and operating cost to be predicted.
Efficiency should be evaluated as cost per unit volume treated to the target concentration, accounting for capital, media replacement or energy, and residuals management — not as removal percentage alone.
All separation technologies produce a PFAS-containing residual — spent carbon, spent resin, or membrane concentrate. The treatment system is not complete until that residual has a defined, acceptable disposal or destruction route.
Systems designed from site-specific pilot data, with lead-lag vessel configurations and monitoring between vessels, consistently perform more predictably than those sized from generic assumptions. Where short-chain PFAS are significant, combined approaches such as GAC followed by ion exchange let each medium handle the compounds it removes most economically.
How these considerations combine into complete process configurations is covered in our guide to the PFAS treatment train.
Efficiency considerations differ between drinking water and wastewater applications. Drinking water systems face very low concentration limits and relatively clean source water, a context addressed in our guide to drinking water PFAS removal systems. Wastewater brings higher and more variable PFAS concentrations and far higher organic loading that competes for adsorption, as covered in our discussion of wastewater PFAS treatment.
Development is focused on adsorbents with greater selectivity for short-chain PFAS, regenerable media, and destruction technologies for the concentrated residuals that removal technologies produce. Biological treatment has not been shown to degrade perfluorinated compounds such as PFOA and PFOS at practical rates.
Federal requirements are in flux, and several states maintain their own PFAS standards. Designing for measured source water quality and realistic breakthrough behavior provides a robust basis regardless of how regulations evolve.
PFAS removal efficiency is not a single number. For adsorptive media it is a function of time, compound, and water chemistry, best described by breakthrough curves developed on the actual source water. For membranes it is more stable but comes with a concentrated residual. Conventional treatment and conventional advanced oxidation remove little PFAS.
Evaluating technologies on bed life for the limiting compound, cost per unit volume treated to target, and residuals management provides a far sounder basis for decisions than headline percentages. Those measures, established through pilot testing, are the foundation of effective and economical PFAS treatment.