Open access
State-of-the-Art Reviews
Oct 28, 2021

Per- and Polyfluoroalkyl Substances Presence, Pathways, and Cycling through Drinking Water and Wastewater Treatment

Publication: Journal of Environmental Engineering
Volume 148, Issue 1

Abstract

Per- and polyfluoroalkyl substances (PFAS) are compounds of emerging concern based on ubiquitous distribution and potential human health impacts. Whereas manufacturing plants and fire-training/suppression areas are recognized as primary sources of PFAS contamination of the environment, understanding the role of water treatment plants (WTPs) and water resource recovery facilities (WRRFs) in PFAS cycling is important. Literature on the presence and pathways of PFAS within and between WTPs and WRRFs was reviewed and synthesized to address this knowledge gap. The production, use, and disposal of PFAS was connected to the water cycle via aquifers/surface water/sediment, drinking water treatment, domestic/industrial water use, domestic/industrial wastewater treatment, the atmosphere, land application, landfills, thermal treatment of wastes, and food production. WTP and WRRF flows release PFAS in liquid-phase, solid-phase, and gas-phase matrices. The purpose of this review is to educate and inform readers of the fate and transport of PFASs throughout the urban water cycle emphasizing the WTP–WRRF connection. Source reduction programs, treatments that interrupt the PFAS cycle, and comprehensive analytical methods are future research needs.

Introduction

Per- and polyfluoroalkyl substances (PFAS) present a unique challenge in water and wastewater treatment (Vo et al. 2020). Conventional physicochemical and biological treatment methods cannot fully degrade or mineralize PFASs in drinking water treatment (Belkouteb et al. 2020; Kim et al. 2020; Boone et al. 2019; Dauchy 2019; Page et al. 2019; Vughs et al. 2019; Hopkins et al. 2018) or wastewater treatment (Chen et al. 2018; Szabo et al. 2018; Arvaniti and Stasinakis 2015) and may generate PFAS transformation products. The treatment goal of mineralization relative to PFAS is defined by Horst et al. (2020) as complete defluorination regardless of whether the carbon is fully oxidized to carbon dioxide. In contrast to conventional treatment methods, Ahmed et al. (2020a) published a critical overview of different advanced degradation methods—advanced oxidation, PFAS defluorination, advanced reduction, and thermal and nonthermal processes—for PFAS removal from water and wastewater. However, the authors noted that most of these methods are laboratory studies at this stage that show promise but have not been tested in real commercial-scale plants.
Fluorine, the lightest halogen, is the most electronegative element; as such, the C–F bond is among the strongest of known covalent bonds (Kissa 2001). Properties of PFAS are useful for industrial and commercial purposes, and mass production has occurred since the early 1950s (Kissa 2001). The same properties, such as thermal stability and chemical inertness, that make them useful also make them stable and environmentally persistent. As production continued into this century, environmental accumulation of PFAS from intentional and nonintentional releases has occurred. For instance, PFAS utilized in specific firefighting foams are distinct sources of environmental PFAS (Dauchy 2019). More broadly, the USEPA states that manufacturing plants, fire-training areas, and fire-suppression activities at airports, refineries, and military installations are primary sources of PFAS release to the environment (USEPA 2021a).
The USEPA maintains an online, continuously growing (currently >9,000 chemicals) master list of PFAS (USEPA 2021b). Multiple categories of perfluoroalkyl (fully fluorinated carbon atoms) and polyfluoroalkyl (partially fluorinated carbon atoms) compounds exist. Each PFAS has a linear or branched alkyl chain (Kissa 2001) and a perfluoroalkyl group (CnF2  n+1) (Buck et al. 2011). Detailed definitions of PFAS-related terminology are available in Buck et al. (2011), Dauchy (2019), Pancras et al. (2016), and Wang et al. (2017). PFAS diversity is tabulated in Winchell et al. (2021a), and representative chemical structures are illustrated in Winchell et al. (2021b). PFAS comprise a large family of chemicals cataloged across various nomenclatures such as (1) polymeric (including fluoropolymers, perfluoropolyethers, and side-chain fluorinated polymers) and nonpolymeric [including perfluoroalkyl acids and per-/polyfluoroalkylether acids (PFAA), PFAA precursors, and others], most of which are further subcategorized; (2) legacy, transformation products, and emerging PFAS; (3) ultrashort-, short-, and long-chain PFAS; and (4) polar/nonpolar, nonvolatile/semivolatile/volatile, and neutral/anionic/cationic/zwitterionic PFAS. PFAA precursors are fluorinated chemicals that can be transformed abiotically or biotically into terminal perfluoroalkyl carboxylic acid (PFCA) or perfluoroalkyl sulfonic acid (PFSA) products (Casson and Chiang 2018).
In 2006, the USEPA initiated the 2010/2015 PFOA Stewardship Program, inviting eight major PFAS industries to work toward the elimination of perfluorooctanoic acid (PFOA), PFOA precursor chemicals, and related higher homolog chemicals. The program is one of the main drivers of the reformulation of PFAS-based products. All companies have met the PFOA Stewardship Program goals (USEPA 2021c). The Stockholm Convention has restricted the production of perfluorooctanesulfonic acid (PFOS) (UNEP 2019a) and banned the production of PFOA (UNEP 2019b). However, as will be confirmed in this review, these PFAS still occur in the water cycle because of their persistence and because importation from other global markets remains a route for material entering the domestic chain of commerce.
In response to increased regulation of long-chain so-called legacy PFAS [eight or more carbons (C8) in the alkyl chain and no ether bonds], industrial applications have shifted toward short-chain (C4–C7) and ultrashort-chain (C2 and C3) PFAS alternatives, with or without ether bonds (Wang et al. 2019; Mulabagal et al. 2018). As reported by the Interstate Technology and Regulatory Council (ITRC 2020), alternative PFAS-based chemical replacements are being marketed and some are appearing in the environment (Munoz et al. 2019; Gustavsson et al. 2018; Hopkins et al. 2018; Wang et al. 2015b), especially several subclasses of ether-PFASs, including the most well-known F-53B [major component (9-chlorohexadecafluoro-3-oxanonane-1-sulfonic acid) or 9Cl-PF3ONS and minor component (11-chloroeicosafluoro-3-oxaundecane-1-sulfonic acid) or 11Cl-PF3OUdS], Gen-X (hexafluoropropylene oxide dimer acid or HFPO-DA), and ADONA (4,8-dioxa-3H-perfluorononanoic acid) compounds (named in their acid forms). These PFAS replacement chemicals are now included in the EPA Analytical methods 533 and 537.1 for PFAS in drinking water (USEPA 2019). Unfortunately, many recently adopted fluorinated alternatives and precursors are more persistent and more environmentally mobile than legacy PFAS (Ghisi et al. 2019).
Broad environmental PFOS contamination has been documented. Giesy and Kannan (2001) were the first to report global PFOS contamination in wildlife. For example, PFOS concentrations in the Midwestern US was as high as 2,570  ng/mL in the blood plasma of bald eagles and 3,680  ng/g wet weight in liver samples from mink. Animals tested from urban areas yielded higher concentrations than more remote locations; even wild polar bears contained detectable levels of PFOS. PFOS was measured at higher concentrations in predator species than prey, suggesting bioaccumulation of PFOS. A follow-up study demonstrated bioaccumulation in aquatic species (Giesy et al. 2010) and estimated water quality criteria for the protection of aquatic organisms and wildlife.
Several studies across the globe have recently been published to illustrate the broad environmental contamination of PFAS. Muir et al. (2019) documented the wide presence of PFASs throughout the Arctic Ocean and near-shore environments, but they noted that “most long-term time series show a decline from higher concentrations in the early 2000s.” Ali et al. (2021) measured Saudi Arabian Red Sea PFAS concentrations in sediments and edible fish and pointed to wastewater effluents as the main source of these compounds. Bai and Son (2021) performed a study investigating the presence of 17 specific PFAS compounds in 6 surface water and sediment locations in the US state of Nevada, and found that short-chain PFAS were more prevalent in the aqueous phase, while long-chain PFAS were more prevalent in soil (sediments). Cao et al. (2019) investigated soil, sediment, and aqueous-phase PFAS in the Yuqiao reservoir in Tianjin, China, while Chen et al. (2021) investigated similar environmental samples in the Pearl River in southern China. Additional local studies across the globe regarding PFAS environmental contamination include Florida (Cui et al. 2020), Kampala, Uganda (Dalahmeh et al. 2018), Three Gorges Reservoir, China (Jin et al. 2020), the Asan Lake region of South Korea (Lee et al. 2020), South African estuaries (Olisah et al. 2021), Beibu Gulf, South China (Pan et al. 2021), Gangetic Plain, Patna, India (Richards et al. 2021), Mexico City (Rodríguez-Varela et al. 2021), Xiamen Bay, China (Wang et al. 2020), and the Loess Plateau, China (Zhou et al. 2021).
In soils, Brusseau et al. (2020) compiled data from more than 30,000 samples from over 2,500 sites globally; the maximum reported PFOS concentrations reached up to several hundred milligrams per kilogram, even in remote regions, where sites were far from PFOS sources. Zacs and Bartkevics (2016) measured PFOA and PFOS in surface water, wastewater, biota, sediments, and sewage sludge in the Baltic region. They noted a prevalence of PFOS over PFOA in surface water and biota samples, whereas mean concentrations of PFOA were greater than PFOS in wastewater, sediments, and sewage sludge. Other, recent, reviews focused on fate and transport within soils and sediments, such as Willemsen and Bourg (2021), who studied the adsorption kinetics of various PFAS structures. Ahmed et al. (2020b) noted decreasing adsorption onto activated carbon as the carbon chain length increased in PFAS, although longer-chain PFAS have larger partition coefficient values than shorter-chained versions. Using numerical studies of PFOS transport within unsaturated soil, researchers have concluded that groundwater contamination could occur from decades to centuries after an initial surface spill (Mahinroosta et al. 2021; Sánchez-Soberón et al. 2020).
A growing body of literature has demonstrated that PFAS are found in nearly all environments and in the organisms living therein, including humans. There are now thousands of research reports on the occurrence of PFAS in humans, with data being reported on PFAS levels in human blood, urine, milk, and other tissues (hair and nails) (De Silva et al. 2021; Liu et al. 2020; Jian et al. 2018). While most studies, to date, have focused on human blood, more recent research indicates the distribution of PFAS in various tissues is a function of both PFAS chain length and physiological characteristics (Jian et al. 2018).
Water and diet are major potential pathways of PFAS exposure in humans along with food packaging, cookware, air, and air-suspended dust (Ghisi et al. 2019). Elevated PFAS water contamination from localized sources can impact raw water, and thus consumption of contaminated drinking water is a major pathway for human exposure (Tröger et al. 2021; Appleman et al. 2014) if PFAS-specific drinking water treatment is not implemented. The USEPA has established the drinking water health advisory level (HAL) at 70 parts per trillion (combined concentrations of PFOA and PFOS) (USEPA 2016). If drinking water meets the USEPA HAL, the daily intake of PFOS and PFOA from water is less than 20% of the estimated total average human intake per day (USEPA 2016).
PFAS contamination of food may occur via irrigation and biosolid application in agriculture (Ghisi et al. 2019) and home food production (Huset and Barry 2018) or farmed and hunted animals (Death et al. 2021), resulting in additional human exposure. Ramakrishnan et al. (2021) documented the presence of PFAS even within organic farming systems and produce production. They noted the use of PFAS-containing composts and feeds, and report that, in some instances, organic meats may contain even higher concentrations of select chemicals than conventionally grown produce. With ubiquitous contamination and bioaccumulation tendencies, growing public concern about human exposure to PFAS stems from an increasing body of evidence of adverse toxicological effects (Sunderland et al. 2019; ATSDR 2021).
Given the concern and broad environmental impact of PFAS, this manuscript aims to establish the connections within and between water resource recovery facilities (WRRFs) and drinking water treatment plants (WTPs) including their role in the fate and transport of PFAS cycling in the environment in a manner to inform the industry on this issue. The term water resource recovery facility is adopted here instead of wastewater treatment plant (WWTP) to more broadly reflect the ability to recover valuable resources from wastewater as advocated by the Water Environment Federation (WEF) (WEF 2014). Evidence for PFAS cycling is presented to inform and educate students, professional engineers, scientists, lab managers, treatment plant operators, and decision makers interested in the status of PFAS water quality impacts.

PFAS Cycling

To understand potential human exposure to PFAS, it is necessary to thoroughly evaluate the PFAS cycle, including WTPs and WRRFs (AWWA 2020). While significant research has focused on the occurrence of PFAS in portions of the water cycle, comprehensive discussions of the complete cycle are limited, as discussed herein. Vo et al. (2020) recently contributed a review of PFAS sources and their occurrence, transformation, fate, migration, and remediation that addresses technologies in both water and wastewater.
In this manuscript, a different approach to investigating the water/wastewater cycle through the environment is made by examining the three phases of matter (i.e., liquid, solid, and gaseous) in which PFAS are transported. Each phase may contribute to overall human exposure via different routes prior to returning to the WTP or WRRF.
The production, use, and disposal of PFAS connects to the water cycle via aquifers/surface water/sediment, drinking water treatment, domestic/industrial water use, domestic/industrial wastewater treatment, the atmosphere, land application, landfills, thermal treatment of wastes, and food production (Fig. 1). In Fig. 1, outputs from PFAS primary sources are depicted by densely dotted lines. Each arrowhead in Fig. 1 represents an input to a different environmental compartment.
Fig. 1. PFAS cycling in water and wastewater treatment. Environmental compartments are depicted in rectangles. Potential significant human exposure points are denoted by rectangles with filled backgrounds. The primary PFAS environmental release paths from PFAS production/use/disposal are represented by thick dotted lines. Output paths are indicated for the gas phase (dashed line), liquid phase (loosely dotted line), and solid phase (solid line). Each arrowhead represents a source to a different environmental compartment.
Here we focus on WTPs and WRRFs as an integrated anthropogenic system composed of multiple unit operations that result in aqueous (loosely dotted lines), solids (solid lines), and gaseous (dashed lines) discharges of legacy, replacement, and transformed PFAS to the environment (Fig. 1). In addition to cycling within these phases, phase-transfer processes, i.e., solids–air, solids–water, and air–water partitioning, are also important in the transport and fate of PFAS (Brusseau 2019a, b).

Liquid-Phase Path

Liquid-phase PFAS-containing inputs continuously enter WTP and WRRF facilities (liquid-phase path, loosely dotted lines, Fig. 1). WTPs are fed from groundwater and surface water. WRRFs are fed used WTP water, wastewater from untreated domestic, commercial, and industrial sources—including from PFAS production, internal recycling of spent streams, inflow and infiltration, and landfill leachate discharges to sanitary sewers. Dry and wet deposition can result in PFAS contamination (Pike et al. 2021). Chen et al. (2019) collected water from precipitation events in urban China and measured 22 PFAS reporting that trifluoroacetate (TFA), PFOA, and PFOS were the predominant PFAS.
WTP outputs, which often become WRRF inputs, directly impact human exposure by supplying drinking water for human consumption and irrigation for home garden food production (Huset and Barry 2018). WRRFs return treated effluents to surface water and indirectly to aquifers that become inputs to WTPs, completing the urban water cycle. Once in the aquatic environment, bioaccumulation and biomagnification of these compounds can lead to human exposure through consumption of fish and wildlife (Fair et al. 2019).

Presence in Drinking Water Supplies

Legacy and replacement PFAS have been measured in surface and groundwater supplies of drinking water (Kumarasamy et al. 2020; Mullin et al. 2019; Dauchy et al. 2017; Zaggia et al. 2016). Guelfo and Adamson (2018) examined the USEPA nationwide screening of PFAS and reported that groundwater represented 72% of all samples where PFAS detections occurred.
Urban and industrial discharges (Campo et al. 2016), aqueous film-forming foam (Daly et al. 2018), use of recycled water from WRRF effluent to irrigate crops on agricultural land (Szabo et al. 2018), managed aquifer recharge of recycled water and urban stormwater (Page et al. 2019), and land application of wastewater biosolids (USEPA 2020) are potential sources of PFAS to drinking water supplies.
Source identification of PFAS contamination in groundwater in nonindustrial areas suggested that domestic sewage and atmospheric deposition may contribute significantly (Wei et al. 2018). Hu et al. (2016) reported on PFAS in US drinking water affected by WRRF effluents and found that the presence of WRRFs is a significant predictor of PFAS detection frequencies and concentrations in public drinking water supplies.
Clara et al. (2009) found PFAS in surface water and sediment, reporting that up to 50% of PFAS contributions are from wastewater discharges. They also noted other impacts from point source emissions, degradation of precursor products, runoff from contaminated sites, and dry and wet atmospheric deposition.

Removal through Drinking Water Treatment

If present in source water, PFAS are not substantially removed by most conventional water-treatment technologies, including coagulation, flocculation, sedimentation, filtration, and chlorine disinfection (Belkouteb et al. 2020; Kim et al. 2020; Boone et al. 2019; Dauchy 2019; Page et al. 2019; Vughs et al. 2019; Hopkins et al. 2018). In addition to being poorly removed by conventional processes, a review of advanced technologies (Rahman et al. 2014) reported that biofiltration, oxidation (either ozonation or advanced oxidation), ultraviolet (UV) irradiation, and low-pressure membranes were all poor methods for elimination of PFAS. Hopkins et al. (2018) also reported that GenX—a PFOA replacement—and other per- and polyfluoroalkyl ether acid replacement PFAS were not measurably removed by ozonation, biofiltration, and disinfection using medium-pressure UV lamps. Interestingly, Boiteux et al. (2017) reported that ozonation increased the concentration of certain PFAS. If PFAS are inefficiently removed from contaminated source water, they will remain in finished drinking water and will result in a primary exposure route for human populations (Binetti et al. 2019; Boiteux et al. 2017).
PFAS are well removed through various separation methods such as granular activated carbon (GAC), ion exchange (IX), or nanofiltration/reverse osmosis (NF/RO) membranes (Belkouteb et al. 2020; Kim et al. 2020; Li et al. 2020; Rodowa et al. 2020; Ateia et al. 2019a, b; Boone et al. 2019; Page et al. 2019; Patterson et al. 2019; Wei et al. 2019; Hopkins et al. 2018; Schaefer et al. 2018; McCleaf et al. 2017; Zaggia et al. 2016; Appleman et al. 2014; Rahman et al. 2014). Gagliano et al. (2020) reviewed the removal of long- and short-chain PFAS by adsorption and noted that the adsorption capacity of short-chain PFAS is lower than that observed for long-chain PFAS. While these separation methods have been shown to remove PFAS from drinking water, they subsequently generate PFAS-contaminated residuals.
Regeneration of anion exchange resins from drinking water treatment generates PFAS side streams that require further treatment prior to disposal (Page et al. 2019; Schaefer et al. 2018; Rahman et al. 2014). GAC and other spent resins used in drinking water treatment processes can be regenerated, landfilled, thermally reactivated, or incinerated (Hopkins et al. 2018). Membrane concentrates are liquids that may be disposed of by marine or deep well discharges, but these options do not break the PFAS cycle. A possible solution for destroying membrane concentrates, employed by some municipal solid waste facilities, is incineration, which has been used for membrane concentrates from leachate (Ren et al. 2020, 2019). Although incineration holds promise for the destruction of PFAS residuals, incomplete mineralization could lead to air emissions (Winchell et al. 2021a).

Wastewater

WRRFs are both sinks and sources of PFAS contamination (Chen et al. 2018) and may release PFAS into the environment (Wang et al. 2018). Relatively large flows of wastewater (Kwon et al. 2017; Arvaniti and Stasinakis 2015) and urban stormwater (Page et al. 2019) are important in environmental PFAS cycling because conventional treatment processes at WRRFs remove very little PFAS and stormwater often receives no treatment. Hamid et al. (2018) previously published a review of the role of WRRFs in the environmental cycling of PFAS through aqueous effluent, sludge, and air emissions.
Conventional WRRFs have demonstrated limited effectiveness in removing PFAS from the aqueous phase (Arvaniti and Stasinakis 2015; Chen et al. 2018; Szabo et al. 2018). Observations that selected PFAS concentrations increase across WRRFs has been reported, albeit it with variable results (Lenka et al. 2021; Choi et al. 2019; Coggan et al. 2019; Seo et al. 2019; Gallen et al. 2018; Wang et al. 2018; Eriksson et al. 2017; Kwon et al. 2017; Hamid and Li 2016; Houtz et al. 2016; Arvaniti and Stasinakis 2015; Loos et al. 2013; Venkatesan and Halden 2013; Yu et al. 2009; Loganathan et al. 2007; Schultz et al. 2006). The increases in PFAS concentrations during treatment are attributed to breakdown of unmeasurable precursors such as fluorotelomer alcohols (FTOH), perfluoroalkyl phosphates (PAPS), or fluorotelomer sulfonates (FTS) in the wastewater treatment process and yield measurable PFAS byproducts (Zhang et al. 2021; Eriksson et al. 2017; Loganathan et al. 2007).
WRRFs pass PFAS to surface waters (Seo et al. 2019; Rahman et al. 2014) and to the atmosphere via aeration and clarifiers that are open to the air (Dimzon et al. 2017; Ahrens et al. 2011). Because WRRFs do not destroy PFAS through treatment, the pass through sets up a potential recycle to downstream drinking water treatment facilities, which may draw source water from wastewater effluent impacted receiving streams (Wells et al. 2017).

Solid-Phase Path

Residuals and solids (solid-phase path, solid lines, Fig. 1) generated at WTPs and WRRFs, respectively, can be land applied for beneficial reuse, sent to a landfill, or subjected to thermal treatment or incineration. Residuals from water treatment have been shown to contain PFAS (Coggan et al. 2019; Lazcano et al. 2019; Nakayama et al. 2019; Rainey 2019; Seo et al. 2019; Eriksson et al. 2017; Gallen et al. 2017; Kwon et al. 2017; Mailler et al. 2017; Armstrong et al. 2016; Pan et al. 2016; Ulrich et al. 2016; Alder and van der Voet 2015; Wang et al. 2015b; Yan et al. 2012; Navarro et al. 2011; Sun et al. 2011; Guo et al. 2010; Loganathan et al. 2007). Sediments from surface waters have been shown to contain PFAS that have been linked to WRRF effluent (Mussabek et al. 2019; Bach et al. 2017; Qi et al. 2017). Ash from inefficient incineration processes (Loganathan et al. 2007) may also be another potential input to PFAS cycling in the environment.

Residual Solids

Based on 2019 data (USEPA 2020) from major publicly owned treatment works (POTWs) or WRRFs, the disposition of residual solids was land application (51%), landfilling (22%), incineration (16%), other management practices (10%), and surface disposal (1%). Solids from WTPs are primarily sent directly to WRRFs or landfills, with some land application of residuals (USEPA 2011). Solids generated in WTPs and WRRFs may undergo further treatment at wastewater treatment facilities to stabilize the solids, reduce mass, and inactivate pathogens. Sáez et al. (2008) studied bacterial degradation of PFAS under aerobic and anaerobic conditions in municipal WRRF solids, observing no PFAS degradation. Lazcano et al. (2019) observed no change in specific PFAS content for wastewater solids through composting or drying processes. Several studies have documented PFAS concentrations in digested solids, termed biosolids, once pathogen reduction reaches levels required for beneficial reuse (Rainey 2019; Alder and van der Voet 2015; Sun et al. 2011).
PFAS partition from wastewater to sorb onto solids (Choi et al. 2019; Guo et al. 2010). Loganathan et al. (2007) found that suspended solid samples contained higher concentrations of PFOS than did the bulk liquid filtrate at the WRRFs investigated. Differences in the distribution of PFAS between liquids and solids were assessed by Eriksson et al. (2017) using a distribution coefficient. Generally, the distribution coefficient increases with chain length; however, electrostatic interactions were hypothesized to be more critical than hydrophobic interactions for the sorption of shorter-chained PFAS (C5).
Organic characteristics of solids were demonstrated to be crucial to the sorption of PFAS (Wang et al. 2015a). The authors determined that an activated sludge with a higher content of biological organics had greater affinity than primary treatment solids for PFAS.
Pan et al. (2016) reported that the congener distribution pattern of PFAS in solids was different than in the aqueous phase. Eriksson et al. (2017) also found that the PFAS profile in solids differed from the profile in effluent, both in compound class composition and homolog chain length. Hamid et al. (2018) reported that long-chain PFCA (>C8) were primarily detected in the solid phase. However, Yan et al. (2012) found that concentrations of short-chain PFAS (<C6) were also abundant in WRRF solids. Significant contamination of PFAAs (Lee et al. 2014) as well as PFCA, PFSA, and perfluoroalkane sulfonamides (FOSA) (Hamid and Li 2016) have been documented in WRRF solids. Eriksson et al. (2017) reported that of the several classes of precursors, intermediates, and persistent PFAS in solid samples, the vast majority were precursor compounds and intermediates. Many diverse PFAS occur in solids and differ from PFAS in aqueous phases.

Landfills

PFAS-containing solid and liquid wastes derived from residential, commercial, and industrial sources have been disposed in landfills for decades (Masoner et al. 2020; Scher et al. 2018; Seo et al. 2019). Inputs to landfills are also anticipated from wastes generated in the WTP/WRRF cycle, including disposal of PFAS contaminated GAC, sludges, and residual solids from thermal treatment (Page et al. 2019; Kwon et al. 2017).
Landfills contribute the continuous release of PFAS to the environment where certain PFAS transfer into the leachate, which is often sent to wastewater facilities for treatment (Masoner et al. 2020; Solo-Gabriele et al. 2020; Wei et al. 2019; Gallen et al. 2017; Busch et al. 2010). Wei et al. (2019) indicated PFAS treatment in landfill leachates can be complicated by the presence of other pollutants such as dissolved organic matter, fulvic-like and humic-like compounds, xenobiotic organic compounds, heavy metals, and inorganic salts. Treatment methods for leachate include physical separation (adsorption, resin, and membrane filtration), oxidation, reduction, or thermolysis. Although landfills were intended to be the final stage in the PFAS lifecycle (Wei et al. 2019; Lang et al. 2017), research has demonstrated this is not the case (Harrad et al. 2020; Ghisi et al. 2019; Hepburn et al. 2019; Riedel et al. 2019). Outputs from landfills can contaminate water (leachate) and air, discussed in the liquid-phase and gas-phase sections of this review, respectively. Information is lacking on the distribution, transformation, and fate of PFAS in landfills (Wei et al. 2019). Leachate from unlined landfills may impact groundwater (Harrad et al. 2020). Additionally, PFAS in landfill leachate that is collected and disposed in WRRFs, a common practice for landfill leachate management, may either pass through the WRRF or sequester in biosolids, which are commonly land applied (Masoner et al. 2020). Contributions of gas-phase emissions from landfills may be significant but are rarely measured due to analytical constraints on field sample collection (primarily limited to offline analyses of liquid-phase extracts) and quantification (analyses in which volatile or semivolatile PFAS may be lost) (Riedel et al. 2019).

Land Application

Solids generated at WTPs and WRRFs are often beneficially land applied as soil conditioners (Ghisi et al. 2019). Wastewater solids applied to agricultural land have beneficial purposes as fertilizers (Yan et al. 2012). WTPs using lime softening generate calcium-rich solids that are often sent to WRRFs, landfilled, or used in agricultural practice as a liming agent. However, these solids may have some PFAS contamination that would coincidentally be land applied, even if biosolids have been thermally treated to be considered exceptional quality Class A by USEPA standards (Lazcano et al. 2019). Assessing PFAS precursors when wastewater solids are applied in agriculture is very important because, once applied to the soil, precursors can be degraded and increase PFAA concentrations (Lazcano et al. 2020; Zhang et al. 2019; Valsecchi et al. 2013; Vestergren et al. 2012; Ellington et al. 2009).
The beneficial results from the land application of wastewater solids may be complicated by the presence of PFAS contamination and the potential for bioaccumulation of PFAS in agricultural plants (Ghisi et al. 2019). Zhang et al. (2020) investigated soil adsorption and plant bioaccumulation in water–soil–aquatic plant systems and determined that longer-chain PFAS had a higher affinity for the soil substrate, whereas shorter-chain PFAS were preferentially translocated from roots to shoots. Ghisi et al. (2019) reported that plant uptake of PFAS was directly correlated with PFAS concentrations in soil and was dependent on PFAS chain length, functional group, and plant species/organ. Bolan et al. (2021a, b) reviewed the distribution, fate and transport, and potential remediation techniques of PFAS-containing soils that had received solid biowastes such as biosolids, composted material, and agricultural manure.
Runoff or leaching from biosolid-amended soils can also lead to elevated PFAS levels in receiving waters (Röhler et al. 2021). Navarro et al. (2018) demonstrated that PFAS transferred from biosolid-amended soil to leachate and runoff water generated by natural rainfall, confirming that leaching is possible. In 2011, Lindstrom et al. (2011) described a scenario in Decatur, Alabama, where PFAS-contaminated biosolids from a municipal WRRF that had received waste from local fluorochemical facilities were used as a soil amendment. After over a decade of application, 10 target PFAS were measured in surface and groundwater samples, with many samples exceeding the US EPA HAL for PFOA in drinking water. In another example, trace levels of PFAS were found in cores taken from a biosolid-amended soil at depths of up to 120 cm, suggesting the potential movement of these compounds within the soil profile over time (Sepulvado et al. 2011). The same study also confirmed a higher transport potential for short-chain PFAS in soils amended with municipal biosolids.
PFAS concentrations may need to be considered, along with nutrient (nitrogen and phosphorus) concentrations, when calculating application rates of biosolid-based fertilizers as soil amendments. The application rate of a fertilizer is usually based on the nitrogen contents of the soil and the fertilizer. Land application of biosolid-based fertilizers with low PFAS concentration and low nitrogen content could result in a higher PFAS load compared to fertilizers with high PFAS concentration and high nitrogen content (Lazcano et al. 2020).

Activated Carbon

Another solid-phase source of environmental PFAS contamination from water treatment systems is based in the handling of spent activated carbon. Activated carbon adsorbs pollutants and removes PFAS (Appleman et al. 2014; Belkouteb et al. 2020). Once exhausted, the activated carbon must either be disposed, along with its PFAS load, or reactivated. If disposed in a landfill, over time the PFAS may desorb and reenter the water cycle via leachate. Regeneration involves thermal treatment, which drives off, but might not fully destroy, the PFAS (Watanabe et al. 2018, 2016), which may reenter the cycle through atmospheric dispersion or through other residuals produced by thermal processing.
Baghirzade et al. (2021) recently summarized the literature related to the regeneration of PFAS-laden GAC. The authors concluded that thermal regeneration provides dual benefits—breaking the PFAS cycle in the environment while reducing replacement costs of the valuable GAC media. Several bench-scale studies on GAC handling and PFAS contamination have also recently been published. Xiao et al. (2020) examined the thermal stability and decomposition of seven PFCAs, three PFSAs, and one perfluoroalkyl ether carboxylic acid (PFECA) in N2, O2, CO2, and air atmospheres on spent GAC. In this laboratory spiking study, the researchers concluded that >80% of PFOA and PFOS adsorbed on GAC was converted to fluoride ions at temperatures exceeding 700°C. Concomitantly, initial PFOA and PFOS concentrations were reduced by more than 99.9%. Gagliano et al. (2021) reported that microwave irradiation was promising as an alternative thermal regeneration technique for PFAS-saturated GAC with reduced treatment times compared to conventional thermal regeneration. Sasi et al. (2021) demonstrated that low-temperature thermal PFAS decomposition was accelerated by and pathways were altered in the presence of GAC or other highly porous materials. Interestingly, the porosity of GAC was found to be more influential to PFAS decomposition than the character of its polyaromatic surface. These studies support our earlier hypothesis that PFAS destruction improves with other catalytic materials present (Winchell et al. 2021a).
Knowledge gaps cited in these references exist due to the limited research conducted to date on PFAS reduction associated with spent activated carbon. These gaps include lack of current sampling and analytical capabilities that lead to incomplete consideration of decomposition products (Winchell et al. 2021b).

Gas-Phase Path

Gas-phase emissions of PFAS (gas-phase path, dashed lines, Fig. 1) have been documented across unit processes in WTPs and WRRFs. Both WTPs and WRRFs are in open contact with the atmosphere, and PFAS exist in atmospheric gaseous and particulate matter associated with these processes (Yu et al. 2020b; Barber et al. 2007; Jahnke et al. 2007). Thermal treatments and incineration of wastewater solids also are potential sources of direct gas emissions of PFAS to the atmosphere (Winchell et al. 2021a). Once in the atmosphere, FTOHs likely oxidize to yield PFCAs initiated by reaction with OH radicals (Ellis et al. 2004).
As part of the gas cycle, deposition from the atmosphere also occurs. Global atmospheric PFCA deposition was recently modeled by Thackray et al. (2020). These authors found that the ratio of long-chain to short-chain PFCA increased with distance from sources. This ratio can inform the understanding of PFCA formation due to degradation of precursors.

Volatilization

PFAS are unintended release products of volatilization and aerosol-mediated transport during aeration of water and wastewater, and from landfill inputs to the atmosphere. Elevated PFAS concentrations found near WRRF aeration tanks are believed to be associated with volatilization during aeration (Ahrens et al. 2011). Hamid and Li (2016) compiled literature data for PFAS concentrations in air from aeration tanks and reported them to be elevated at 1.5 to 15 times the concentration of sites not contaminated with WRRF emissions.
Dauchy et al. (2017) analyzed soil samples in the vicinity of an industrial WRRF for PFAS. Soil contamination was reported near the activated sludge aeration basin and the filter press. Contamination near the aeration basin indicated a predominance of longer-chain PFAS suggesting that the more hydrophobic PFAS (not the highly volatile PFAS) were volatilized into aerosols and deposited rapidly onto nearby soil. The authors postulated that soil contamination near the filter press resulted from spillage of sludge cake during loading onto trucks.
Brusseau (2019a, b) investigated interactions of PFAS in multiphase systems at solid–water and air/oil–water interfaces demonstrating that fluorinated compounds have greater surface activities compared to their hydrocarbon counterparts similar in chain length. In this study, a quantitative structure-property relationship (QSPR) model based on the molar volume of PFAS best predicted PFAS interfacial adsorption and distribution. The results showed that PFAS transport in multiphase systems is a function of (1) the PFAS molecular properties, (2) solid medium properties, and (3) the magnitudes and distributions of fluid saturations. These transport mechanisms may explain the possible PFAS cycling by air emissions from water treatment–derived solids stored in landfills proposed by others (Ghisi et al. 2019).

Thermal Treatment/Incineration

Incineration and other thermal processes are well-established destruction strategies for solid waste treatment but may present a pathway for atmospheric PFAS emissions. However, knowledge about the thermal degradation of PFAS during wastewater solid thermal treatment is limited. WRRFs often use incineration to combust solids captured through treatment. PFAS may escape destruction through incineration based on high thermal stability or they may only be partially degraded, yielding compounds of equal concern, but inadequate data exist. Winchell et al. (2021a) presented a literature review on the subject and found no conclusive documentation of the fate of PFAS through incineration systems used by WRRFs.
The treatment of solids through thermal drying, hydrolysis, or incineration has the potential to change the PFAS content of the solids. Mailler et al. (2017) observed some PFOA and PFOS reduction in thermally dried solids at WRRFs in Paris, but the finished product still contained measurable concentrations of these compounds. Lazcano et al. (2019) monitored PFAS through drying, composting, and blending operations and detected no change in concentrations, except what could be attributed to dilution. While PFAS concentrations in thermally dried solids may decline, no publicly available data exist considering the off-gas from the drying process, which is likely the removal pathway (Winchell et al. 2021a).

Future Research Needs

While there are both voluntary and regulatory restrictions and bans on the production of some PFAS globally, destructive treatment methods that can break the PFAS cycle, such as plasma technologies, electrochemistry technologies, and other advanced reduction methods (Ross et al. 2018), represent critical research areas. Some of these technologies, though they hold promise, may be years from commercialization, and PFAS continue to enter and exit WTPs and WRRFs in flows that interconnect in the urban water cycle, with the result that these facilities are important in PFAS cycling into the total environment.
Current water and wastewater treatment methods, such as GAC, IX, and RO, that remove PFAS from one medium and transfer them to another only extend PFAS cycling among liquid-, solid-, and gas-phase paths. Alternative thermal treatment technologies, such as pyrolysis, gasification, and hydrothermal liquefaction of WRRF solids, have demonstrated partial mineralization of PFAS (Winchell et al. 2021a; Yu et al. 2020a). An understanding of the mechanisms and extent of destruction has not been fully developed and deserves further research.
While investigations of aspects of PFAS cycling in water and wastewater treatment and the treatment methods by which to interrupt the PFAS cycle are essential research needs, they are complicated by several factors. Kotthoff and Bücking (2018) identified four major trends challenging future PFAS research: mobility, substitution of regulated substances, increase in structural diversity of existing PFAS molecules, and unknown so-called dark matter.

Mobility

The regulation or ban of long-chain legacy PFAS has driven the introduction of short-chain and ultrashort-chain PFAS alternatives, thereby introducing the problem that shorter-chain PFAS are more mobile in water and leachates, as opposed to the adsorption of longer-chain PFAS to solids. Additionally, very short-chain PFAS are also volatile (Kotthoff and Bücking 2018).

Substitution of Regulated Substances

In the ever-changing PFAS chemical enterprise, slight chemical structural modifications are introduced continuously (Winchell et al. 2021b) to achieve similar chemical characteristics while avoiding current regulations of specific compounds. Such chemical substitutions include oxygen (ethers), hydrogen, chlorine, branching, and cross-linking as in the popular PFOA substitutes ADONA, GenX, and F-53B (Kotthoff and Bücking 2018) discussed earlier in the introduction.

Increase in Structural Diversity of Existing PFAS Molecules

Technical-grade commercial products are often manufactured as mixtures of linear and branched isomers, leading to increased structural diversity. Chemically and microbially mediated intermediate PFAS or transformation products lead to new and unidentified PFAS (Kotthoff and Bücking 2018).

Unknown Dark Matter

Finally, Kotthoff and Bücking (2018) refer to the many unknown PFAS as dark matter. Established analytical methods do not exist for countless degradable polymers and numerous PFAS derivatives. Without them, the identity, quantity, formation pathways, and transformation dynamics of polymers and PFAS precursors are impossible to know. Expanded and validated analytical methods for trace quantitation of PFAS legacy, replacement, and transformation products, including sample processing, extraction, purification, and final analysis, are needed and discussed elsewhere (Winchell et al. 2021b).
Current analytical capabilities are not yet adequate to perform a mass balance of the entire PFAS cycle between WTPs and WRRFs in liquid, solid, and gaseous matrices. The lack of a mass balance across the PFAS cycle is a current data gap and a future research direction (Joudan et al. 2020). The evaluation and mass balance of all input and output streams around these treatment systems is necessary to understand the transformation and transport of PFAS from and to the environment or humans. Mass balances require accurate and precise analytical methods for quantification of PFAS in WTP- and WRRF-related samples, as demonstrated in other media, such as paper and textiles (Robel et al. 2017). Additionally, closing a water cycle mass balance will also require the ability to quantify unknown reactive and transient intermediates and associate covalent binding with biological (Joudan et al. 2020) and potentially environmental macromolecules.

Conclusions

PFAS have been shown to contaminate all aspects of the global ecosystem, and WTPs and WRRFs are no exception. Researchers have detected and documented the mobility of PFAS through all three phases (i.e., gas, liquid, and solid) of all inputs and outputs around WTPs and WRRFs. Neither type of treatment facility frequently utilizes processes to remove and destroy PFAS, though physical separation methods exist for PFAS removal from the liquid phase, and thermal processes applied to residual streams from WTPs and WRRFs offer a potential destruction outlet. Moreover, owing to their recalcitrance, PFAS released to the environment, or even disposed of in landfills, can return to the treatment facilities in an endless cycle. For PFAS already present in the environment, physical separation and combustion provide a commercially relevant destruction technology, while pyrolysis and gasification systems are emerging at full scale, and other wet thermal and nonthermal processes are being examined in laboratory settings for solid- and liquid-phase treatment. Because WTPs and WRRFs are not producers of PFAS but are often publicized as sources of contamination, source reduction of the influent PFAS loads to these facilities will be critical to bringing this global issue under control. To better understand how PFAS move through these engineered systems and identify sources to collaboratively reduce the influent contamination, better analytical capabilities are required to measure the broad spectrum of the chemical class in the complex environmental matrices and at toxicologically relevant concentrations. As regulatory and public pressures mount on PFAS contamination, WTPs and WRRFs offer a logical opportunity to stop the environmental cycling of these chemicals, but much work is required to do so in an efficient, economical, and socially just manner.

Data Availability Statement

No data, models, or code were generated or used during the study.

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Go to Journal of Environmental Engineering
Journal of Environmental Engineering
Volume 148Issue 1January 2022

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Published online: Oct 28, 2021
Published in print: Jan 1, 2022
Discussion open until: Mar 28, 2022

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Associate Engineer, Brown and Caldwell, 30 East 7th St., Suite 2500, St. Paul, MN 55101 (corresponding author). ORCID: https://orcid.org/0000-0003-1666-8681. Email: [email protected]
Martha J. M. Wells
Chemical Consultant, EnviroChem Services, 224 Windsor Dr., Cookeville, TN 38506.
John J. Ross
Associate Engineer, Brown and Caldwell, 100 West Big Beaver Rd., Suite 540, Troy, MI 48084.
Management Professional, Great Lakes Water Authority, 735 Randolph, Suite 1100, Detroit, MI 48226. ORCID: https://orcid.org/0000-0003-3304-2437
John W. Norton Jr., M.ASCE
Director of Energy, Research, and Innovation, Great Lakes Water Authority, 735 Randolph, Suite 1100, Detroit, MI 48226.
Stephen Kuplicki
Operations Manager, Great Lakes Water Authority, 735 Randolph, Suite 1100, Detroit, MI 48226.
Majid Khan
Director of Operations, Great Lakes Water Authority, 735 Randolph, Suite 1100, Detroit, MI 48226.
Katherine Y. Bell
Director of Water Strategy, Brown and Caldwell, 220 Athens Way, Suite 500, Nashville, TN 37228.

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