In Situ Sequestration of Per- and Polyfluoroalkyl Substances (PFAS) from Contaminated Groundwater

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In Situ Sequestration of Per- and Polyfluoroalkyl Substances (PFAS) from Contaminated Groundwater Kurt Pennell, Ph.D., P.E. Professor, Brown University Chen Liu (Brown), Yousef Aly, (UMinn), Jennifer Guelfo (Brown), Bonnie Lyon-Marion (Tufts), Natalie Capiro (Tufts), Bill Arnold (UMinn), Jim Hatton (Jacobs), Matt Simcik (UMinn)

PFAS: A Perfect Storm (Irma) Persistent Conventional in situ technologies are not well suited for PFAS: PFOA Mobile Puerto Rico USVI BVI Toxicity C-F bond: ~ 450 kj/mole Widespread Use Hydrophilic head group Hydrophobic/lipophilic tail Bioaccumulation Analytical Capabilities Low Volatility (Thermal) Recalcitrant (Bioremediation, ISCO) Surfactant (Interfaces/Sorption?) 2

Technology Potential PFAS Treatment Options Summary of PFAS Treatment PFOA PFOS Application Chemical Oxidation YES 1,2,3,4 Partial 4 Ex-Situ (Reactor) In-Situ (?) Chemical Reduction YES 5,6 Partial 5,6 Ex-Situ (Reactor) In-Situ (?) Electrochemical YES 7,8 YES 7 Ex-Situ (Reactor) In-Situ (?) Sorption/Sequestration YES 9,10 YES 9,10 Ex-Situ (GAC/Resin) In-Situ (Injection/Barrier Wall) Biological Treatment NO NO Unlikely, PFAS may inhibit chlorinated solvent degradation 1 Liu et al. 2012, Sep and Purf Tech: Heat-activated persulfate 2 Mitchell et al 2013, ES&T Letters: Catalyzed hydrogen peroxide 3 Vecitis et al. 2009, Front. Environ. Sci. Engin. China: UV with TiO 2 4 Park et al., 2016, Chemosphere: Heat-activated persulfate 5 Ochoa-Herrera et al. 2008, ES&T: Ti(III)-citrate and Vit B 12 6 Wang et al., 2017, Chem. Eng. J., Photocatalytic reactivity 7 Schaefer et al., 2015, J. Haz. Mater.:TiRuO 2 anode 8 Zhou et al., 2017, J. Electro. Chem.: PbO 2 electrode + PVDF 9 Zhang et al., 2016, Chemosphere: GAC 10 Yu et al., 2009, Water Res.: GAC and resin 3

Conventional Pump & Treat PFAS Remediation Washington County, MN MN Department of Health/3M 3M Settles Minnesota Lawsuit for $850M (Feb 20, 2018) Breakthrough times: PFBA = 30 days PFOA = 286 days PFOS = 550 days 4

Commercially Available (Proprietary) PFAS Sorbents RemBind -Tersus Activated carbon, aluminum hydroxide, organic matter and other additives, intended for near surface soil mixing PlumeStop Liquid Activated Carbon Regenesis Activated carbon (1-2µm) suspended in water dispersed with organic polymer v Limited independent verification v Limited data (e.g., mass balance) v In situ delivery issues rarely addressed 5

Coagulant polymers (cationic surfactants) SERDP Project ER-2425 (Simcik, Arnold, Pennell, Hatton) Poly-DADMAC (PDM) Accepta 4351 ~ 28% OC Quaternary Amine diallyl dimethylamine MW ~ 350,000 Polyamine (PA) Accepta 4350 ~ 26% OC Quaternary Amine epichlorohydrine and dimethylamine MW ~ 240,000 6

40-50 mesh Ottawa Sand Batch PFAS SorpFon Tests: PDM and PA v Addition of PDM or PA increased PFAS sorption by Ottawa sand and Tinker AFB soil v PFAS Sorption coefficients were 3.8 to 45-fold greater in the presence PDM or PA v PDM yielded slightly greater sorption improvements than PA Aly et al., 2018, J. Env. Eng., (in press)

Electrolyte or PFAS solufon Schematic Diagram of 1-D Column System 3-way valve HPLC Pump Waters Xevo TQ-S Column (2.5x10 cm) Polymer SoluFon FracFon collector Effluent samples analyzed by LC-MS/MS Syringe Pump Side-port InjecFon (1) Non-reactive tracer test (pulse injection), (2) Inject PDM+PAC suspension, (3) Inject background electrolyte, (4) Inject PFAS solution (e.g., 100 ug/l PFOS) 8

PFAS Column Tests: Control (w/o PDM or PA) PFOA (100 µg/l) PFOS (100 µg/l) 40-50 mesh Ottawa sand 40-50 mesh Ottawa sand R F = 1.54 R F = 4.46 Aly et al., 2018, J. Env. Eng., (in press)

Pretreated and Side-Port Co-injecFon: PDM + PFOS Pretreated 40-50 mesh Ottawa sand (100 ug/l PFOS) Side-Port Co-injection 40-50 mesh Ottawa sand (100 ug/l PFOS) Control PA PDM Co-injection initiated TOC PFOS Aly et al., 2018, J. Env. Eng., (in press)

Summary of PFAS Column Results: PDM or PA PFAS RetenFon (ng/g sand) PFAS RetenFon (%) Enhancer retenfon (ng/g sand) Retained PFAS/Retained Enhancer mass rafo PFOA control 5.97 8.95% n/a n/a PDM pre-treatment 8.38 9.50% 21.68 0.11 PA pre-treatment 20.10 21.16% 50.83 0.28 PDM side port injecfon 30.62 49.22% 60.3 0.41 PFOS control 4.20 6.23% n/a n/a PDM pre-treatment 91.94 34.91% 21.68 4.04 PA pre-treatment 43.59 50.04% 77.00 0.51 PDM side port injecfon 196.06 83.22% 42.86 4.47

To improve performance.combine Powdered AcFvated Carbon (PAC) with polydadmac (PDM) 1 g/l PAC v PDM acts to stabilize PAC in suspension, facilitates delivery v Both PDM and PAC can serve as sorbents (wide range of effectiveness) 1 g/l PAC + 5 g/l PDM 1 g/l PAC 1 g/l PAC + 5 g/l PDM DARCO 100 mesh (150 µm) Powdered Activated Carbon (Sigma Aldrich) Immediately after Sonication 48 hrs after Sonication Provisional Patent Application: Reg. No. 41,942, Docket No. 70011-067P01v (September, 2017) 12

PFOA and PFOS Batch Adsorption Studies With Darco PAC (100-mesh) 350 300 PFOA 250 Cs (mg/g) 200 150 100 50 0 0 50 100 150 200 250 300 Ceq (mg/l) Langmuir Isotherm!"=!",$%& '!(,)*/ 1+'!(,)* C s, max = 323 mg/g b = 0.0413 L/mg Cs (mg/g) 400 350 300 250 200 150 100 50 PFOS C s, max = 316 mg/g b = 0.0673 L/mg 0 0 50 100 150 200 250 300 Ceq (mg/l) 13

Injection of PDM+PAC Suspension t = 0 PV ader 3.5 PV PAC+PDM ader 3.5 PV Background Flow Direction 26.8 mg of PAC retained in column 40-50 mesh Ottawa Sand (d 50 = 358 um), k i = 7.37x10-11 m 2, n = 0.37, SSA = 0.0125 m 2 /g, PV = 22 ml PDM+PAC Suspension: 1,000 mg/l PAC + 5,000 mg/l PDM, viscosity = 1.18 cp Flow rate: 0.12 ml/min; pore-water velocity ~1.0 m/day 14

Images of PDM+PAC Treated Ottawa Sand 20X 20 µm 40X Leica DM IL LED

PFOS Column: Control; PDM+PAC treated Ottawa Sand 1.0 0.9 0.8 0.7 0.6 100 µg/l PFOS Control Switch to Background (10 mm NaCl) 40-50 mesh Ohawa Sand v p = 1 m/day C/C0 0.5 0.4 0.3 0.2 0.1 100 µg/l PFOS (PDM+PAC) Increase to 100 mg/l PFOS (PDM+PAC) 0.0 0 5 10 15 20 25 30 35 40 45 Pore volumes 16

Retention of PFOS Mass by PDM+PAC Treated Sand 1.0 0.9 0.8 0.7 43.3 ug PFOS retained 8.31 mg PFOS retained 40-50 mesh Ohawa Sand v p = 1 m/day 0.6 C/C0 0.5 0.4 0.3 0.2 0.1 100 µg/l PFOS (PDM+PAC) Increase to 100 mg/l PFOS (PDM+PAC) 0.0 0.00 5.00 10.00 15.00 20.00 25.00 30.00 35.00 40.00 45.00 Based on the measured C s,max = 316 mg/g and Pore mass volumes of retained PAC (~27 mg), the capacity of the column should be ~ 8.65 mg PFOS, consistent with the observed column retention of ~8.35 mg PFOS For 100 µg/l injection; ~2.1 ug PFOS retained/pv, capacity would be reached after ~4,100 PV

1.0 0.9 0.8 PFOA Column: PDM+PAC treated Ottawa Sand 40-50 mesh Ohawa Sand v p = 1 m/day Switch to Background (10 mm NaCl) 0.7 0.6 C/C0 0.5 0.4 0.3 0.2 0.1 100 µg/l PFOA (PDM+PAC) Increase to 100 mg/l PFOA (PDM+PAC) 0.0 0.00 5.00 10.00 15.00 20.00 25.00 30.00 Pore volumes Based on the measured C s,max = 323 mg/g and mass of retained PAC (~27 mg), the capacity of the column should be ~ 8.72 mg PFOA, consistent with the observed column retention of ~8.48 mg PFOA

Heterogeneous 2.5-D Flow Cell Fully Screened Influent Chamber Constant head influent chamber Background, d 50 =0.36 mm Effluent Chamber Adjustable effluent container Low K layer 1 2.5 x 10 cm low permeable lenses: d 50 = 0.16 or 0.12 mm Low K layer 2 Low permeability bottom layer Dimensions: 40.0 cm (ht) x 63.2 cm (length) x 1.4 cm (thickness) 19

InjecFon of Iron NanoparFcles in Heterogeneous Domain Background velocity = 2 m/d, nmag conc. = 2500 mg/l, gum arabic conc. = 1000 mg/l, injected vol. = 100 ml, background = API brine 20

PFAS InjecFon Ports ConfiguraFon of PFAS 2.5D Flow Cell 40 50 mesh O+awa sand PDM+PAC InjecFon Ports Downgradien t Sampling Ports Soil from Tinker Air Force Base F-90 sand Tinker AFB Soil PV=1.45L F-90 sand 21

Tracer Test Before PDM+PAC InjecFon 22

Side-port InjecFon of 1 g/l PAC + 5 g/l PDM 40 ml (0.08 ml/min) with background flow (2.4 ml/min) 80 ml (0.08 ml/min) with no background flow 23

Tracer Test Ader PDM+PAC InjecFon 24

Collection of PFAS-Impacted Soil & Groundwater Samples Former Loring AFB, Limestone, ME AA07MW02 Std. Dev (ng/ Compound Avg (ng/l) L) PFBA 153.01 11.48 PFPeA 377.77 8.56 PFBS 108.36 2.29 PFHxA 632.10 147.02 4:2-FTS 27.54 9.57 PFHpA 147.78 8.08 PFHxS 1341.42 151.11 PFOA 396.86 17.47 6:2-FTS 1145.98 85.72 PFNA 78.42 29.71 PFOS 1604.65 145.16 PFDA 12.20 11.44 8:2-FTS 98.30 26.13

Conclusions Cationic polymers (PDM or PA) increased PFAS sorption by a factor of 3 to 45 based on batch and column experiments. The combination of powdered activated carbon (PAC) and PDM formed a stable suspension that can be delivered in situ to form a reactive zone. Column and aquifer cell studies demonstrated the sizable capacity of PDM +PAC-treated sand to retain PFOS and PFOA. Future Work Conduct column and aquifer cell experiments with PFAS mixtures, both laboratory prepared and field groundwater samples (Loring AFB) Evaluate the potential release of retained PFAS over time and subject to changing ph and ionic strength. Evaluate competitive effects of NOM and other organic contaminants.

Projects ER-2425 and ER-2714 kurt_pennell@brown.edu 27