A flow-through cell for the electrochemical oxidation of perfluoroalkyl substances in landfill leachates
Graphical abstract
Introduction
Per-and polyfluoroalkyl substances (PFASs) are a group of synthetic chemicals widely used in multiple consumer products (e.g., tapestry, outdoor clothing, cleaning agents, non-stick cookware) and industrial processes (e.g., metal plating, fire-fighting foams, coatings, electronics) due to their unique surface-active properties and high chemical and thermal stability [1,2]. An estimate of 3000 PFASs have been identified, from which perfluorooctanoic acid (PFOA) and perfluorooctanesulfonic acid (PFOS) are two of the most studied compounds [3].
PFASs have triggered attention due to their recalcitrant nature and bioaccumulative potential that leads to their accumulation in water, sediments, soils, wildlife, and the human body [3]. Their exposure and accumulation in the human body have been associated with multiple health effects (e.g., inmunotoxicity, neurotoxicity, testicular and kidney cancer) [4,5]. As a result, the United States Environmental Protection Agency (USEPA) established a health advisory level (HAL) of 0.07 μg/L for the combined concentration of PFOA and PFOS in drinking water [6,7].
Multiple PFASs end their life cycle in landfills as municipal solid waste, and their presence has been reported in landfill leachates in a wide range of concentrations [8,9]. In 2013, for example, a range of 0.15–9.2 μg/L of PFOA was detected in 13 landfill leachate sites in the U.S [8]. A more recent study (2019), performed in Michigan U.S., estimated a daily flow of leachates from 32 landfills of over 1 million gallons with concentrations in the range of 16–3200 ng/L for PFOA and 9–960 ng/L for PFOS [10]. The concentration of PFASs in leachates is affected by various factors, including the heterogeneity of the waste disposed, climate, waste age, and seasonal variability in infiltration [8,9]. According to Lang et al., the most common PFASs present in landfill leachates in the U.S. are 5:3 fluorotelomer carboxylic acid (5:3 FTCA), perfluorohexanoic acid (PFHxA), perfluorobutanoic acid (PFBA), PFOA, 6:2 fluorotelomer carboxylic acid (6:2 FTCA), and perfluoropentanoic acid (PFPeA) [8]. Overall, PFASs ranging from C4-C8 chain length dominate the distribution profiles [11].
Wastewater treatment plants (WWTPs) receive landfill leachates as influents to be treated conventionally. Masoner et al. estimated that although landfill leachates accounted for only 1.7% of the total daily flow that goes into the studied WWTPs, the contribution of total PFASs corresponded to 18% of the total PFASs present in the influent of WWTPs [12]. In addition, previous studies have shown higher concentrations of PFASs in the effluent compared to the influent [8,13]. This observation has been attributed to: 1) the non-biodegradability of PFAS; and 2) the fact that multiple polyfluoroalkyl substances (i.e., precursor compounds) can be further oxidized to perfluoroalkyl substances during biological treatment [8,14]. Some of the precursors include fluorotelomer based substances (FTCAs), perfluoroalkyl sulfonamide derivatives (FASAAs), and polyfluoroalkyl phospahate esters (PAPs) [15,16].
Additional treatment technologies, including adsorption with granular activated carbon (GAC) and membrane processes, i.e., nanofiltration (NF) and reverse osmosis (RO), have been proposed to treat PFASs in landfill leachates [3]. However, the complex composition of a landfill leachate makes GAC inefficient, while for the case of membrane processes, the concentrate containing PFASs require further treatment. Therefore, there is an urgent need for a destructive technology to degrade PFASs and break the accumulation cycle generated by other technologies.
Electrochemical oxidation has shown to be a versatile destructive technology due to its capability to degrade a wide range of contaminants, operation at ambient temperature and pressure, and robust performance [17,18]. Additionally, it does not require auxiliary chemicals and can be operated as a decentralized treatment option [18].
Multiple studies have been conducted to explore the electrochemical oxidation of PFASs in synthetic solutions and groundwater, showing promising results [19,20,21]. However, the effectiveness of the process in complex matrices, e.g., landfill leachate, membrane concentrates, and ion exchange regenerate solutions has been scarcely reported. Although the electrochemical oxidation of PFOA and PFOS in landfill leachates has recently been reported [17], multiple other PFAAs, commonly present in leachates, have only been identified but their oxidation has yet to be addressed.
This study explores, for the first time, the electrochemical oxidation of multiple PFAAs in real landfill leachates using a boron-doped diamond (BDD) flow-through cell. The objectives of this work were to: i) evaluate and compare the degradation kinetics and energy consumption for the electrochemical oxidation of two commonly studied PFASs (PFOA and PFOS) in a synthetic solution with a BDD flow-through cell; ii) assess the electrochemical oxidation of PFAAs in landfill leachates; and iii) determine the influence of leachate composition in the electrochemical oxidation of PFAAs in landfill leachates.
Section snippets
Materials
Perfluorooctanoic acid (PFOA, >97%), heptadecafluorooctanesulfonic acid potassium salt (CF3(CF2)7SO3K, >98%), perfluorobutanoic acid (PFBA, >98%), sodium sulfate (Na2SO4) and sodium chloride (NaCl) were purchased from Sigma Aldrich.
Landfill leachates
Six leachate samples were collected from August 2019 to February 2020 from three different landfills in Michigan, USA. To maintain the confidentiality of sample locations, in this study, leachates were labeled as L1, L2, L3, L4, L5, and L6. The physico-chemical
Performance of the BDD flow-through cell
The electrochemical oxidation of two common PFAAs: PFOA and PFOS in a synthetic solution was evaluated with the flow-through cell. The solution consisted of 70 μg/L of PFOA and 70 μg/L of PFOS dissolved in a 10 mM sodium sulfate (Na2SO4) electrolyte. A current density of 50 mA/cm2 was applied during electrochemical treatment. Fig. 2a shows the decrease in concentration of both PFOA and PFOS over time. Both species followed a pseudo-first order degradation kinetics (r2 = 0.9672 for PFOA and r2
Conclusions
The results presented herein introduced a higher performance cell (flow-through) for the electrochemical oxidation of PFAAs, allowing for lower energy consumption and enhanced mass transfer than a conventional parallel-plate cell.
With the A/V ratio used, current densities equal to or greater than 150 mA/cm2 were necessary to guarantee total PFAAs degradation and avoid a faster generation rate from precursors transformation.
Non-detect levels and degradation > 97% for the electrochemical
Declaration of competing interest
The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.
Acknowledgements
This research project was funded by the City of Grand Rapids (Michigan, U.S.) and Michigan Department of Environment, Great Lakes, and Energy (EGLE). The authors thank Dr. Sibel Uludag-Demirer, Emma Davis, and Marius Ebert for their help with various parts of this research. The authors also thank to Dr. Qi Hua Fan, Dr. Greg Swain, and Dr. Volodomyr Tarabara for their helpful discussions.
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Present address: Geosyntec Consultants, Milwaukee, WI 53202, USA.