Beyond the isotherm: Limits in prediction of PFAS breakthrough behaviour in continuous flow column

Batch kinetic isotherm and continuous flow column experiments were performed for five per- and polyfluoroalkyl substances (PFAS). Coefficient of determination (R 2 ) was higher for Pseudo-Second-Order (PSO, 0.92) than Pseudo-First-Order (PFO, 0.88) kinetic model, suggesting that PFAS removal mechanism was probably based on chemisorption. Freundlich constant (K F ) representing the adsorption capacities revealed that anion exchange resin (AER) consistently outperformed granular activated carbon (GAC) for all tested PFAS. The adsorption capacity of GAC ((mg/g)/(mg/L) 1/n ) increased with increasing chain length from 0.19 for Perfluoropentanoic acid (PFPeA) to 4.94 for perfluoroundecanoic acid (PFUnDA). AER was seen to remove both short and long-chained PFAS effectively. Consistent with that, a clear correlation was observed between the difference in adsorption capacities (ΔK F ) of the adsorbents and PFAS chain length in that AER:GAC adsorption capacity ratio maintained the following order: PFPeA (46) > Perfluorooctanoic acid, PFOA (23.5) > Perfluorononanoic acid, PFNA (8.4) > Perfluorodecanonic acid, PFDA (5.2) > PFUnDA (2.8). This confirms higher adsorption of longer chain PFAS on GAC. In the continuous flow column tests, for GAC, shortest chain PFPeA exhibited the earliest breakthrough at ~7000 bed volumes (BV, day 36), followed by PFOA at ~10,000 BV (day 50). In contrast, PFNA, PFDA, and PFUnDA showed delayed breakthrough at around ~12,000 BV (day 59). For AER, PFPeA again exhibited the earliest breakthrough at ~10,000 BV (day 52), followed by PFOA at ~11,000 BV (day 56) PFDA ~12,000 BV (day 61), PFNA ~13,000 BV (day 66) and PFUnDA~14,000 BV (day 72). The results show that n and K F values measured through batch isotherm tests significantly underestimate the actual breakthrough period observed in continuous flow column experiments. • Adsorption of PFAS on GAC is a function of chain length. • AER consistently outperformed GAC for all PFAS. • Efficiency gap between GAC and AER decreased with increasing PFAS chain length. • Isotherm predicted chain-length dependent trends as in continuous flow columns. • Isotherm underpredicted the service life of the fixed bed continuous flow column.

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Publication Details

Journal
Journal of Water Process Engineering
Published
2025-12-24
DOI
https://doi.org/10.1016/j.jwpe.2025.109352
Primary Topic
Per- and polyfluoroalkyl substances research
Type
article
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article

Beyond the isotherm: Limits in prediction of PFAS breakthrough behaviour in continuous flow column

Céline Kelso, Faisal I. Hai, Mehak Fatima
Journal of Water Process Engineering
Per- and polyfluoroalkyl substances research
article

Beyond the isotherm: Limits in prediction of PFAS breakthrough behaviour in continuous flow column

Céline Kelso, Faisal I. Hai, Mehak Fatima
article en

Abstract

Batch kinetic isotherm and continuous flow column experiments were performed for five per- and polyfluoroalkyl substances (PFAS). Coefficient of determination (R 2 ) was higher for Pseudo-Second-Order (PSO, 0.92) than Pseudo-First-Order (PFO, 0.88) kinetic model, suggesting that PFAS removal mechanism was probably based on chemisorption. Freundlich constant (K F ) representing the adsorption capacities revealed that anion exchange resin (AER) consistently outperformed granular activated carbon (GAC) for all tested PFAS. The adsorption capacity of GAC ((mg/g)/(mg/L) 1/n ) increased with increasing chain length from 0.19 for Perfluoropentanoic acid (PFPeA) to 4.94 for perfluoroundecanoic acid (PFUnDA). AER was seen to remove both short and long-chained PFAS effectively. Consistent with that, a clear correlation was observed between the difference in adsorption capacities (ΔK F ) of the adsorbents and PFAS chain length in that AER:GAC adsorption capacity ratio maintained the following order: PFPeA (46) > Perfluorooctanoic acid, PFOA (23.5) > Perfluorononanoic acid, PFNA (8.4) > Perfluorodecanonic acid, PFDA (5.2) > PFUnDA (2.8). This confirms higher adsorption of longer chain PFAS on GAC. In the continuous flow column tests, for GAC, shortest chain PFPeA exhibited the earliest breakthrough at ~7000 bed volumes (BV, day 36), followed by PFOA at ~10,000 BV (day 50). In contrast, PFNA, PFDA, and PFUnDA showed delayed breakthrough at around ~12,000 BV (day 59). For AER, PFPeA again exhibited the earliest breakthrough at ~10,000 BV (day 52), followed by PFOA at ~11,000 BV (day 56) PFDA ~12,000 BV (day 61), PFNA ~13,000 BV (day 66) and PFUnDA~14,000 BV (day 72). The results show that n and K F values measured through batch isotherm tests significantly underestimate the actual breakthrough period observed in continuous flow column experiments. • Adsorption of PFAS on GAC is a function of chain length. • AER consistently outperformed GAC for all PFAS. • Efficiency gap between GAC and AER decreased with increasing PFAS chain length. • Isotherm predicted chain-length dependent trends as in continuous flow columns. • Isotherm underpredicted the service life of the fixed bed continuous flow column.

Journal of Water Process EngineeringVol. 81
University of Wollongong (AU)
Clean water and sanitation
Openalex Percentile: Top 38%
Per- and polyfluoroalkyl substances research
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