Sampling for monitoring per- and polyfluoroalkyl substances (PFAS) in surface water, groundwater and pore water
11579134 · 2023-02-14
Assignee
Inventors
- Eliza M. Kaltenberg (Quincy, MA, US)
- Franco Pala (Rockland, MA, US)
- Kavitha Dasu (Hanover, MA, US)
- Fred Griesemer (Columbus, OH, US)
- Bradley Westlake (Columbus, OH, US)
- George Nanes (Columbus, OH, US)
Cpc classification
B09C1/00
PERFORMING OPERATIONS; TRANSPORTING
B01J20/262
PERFORMING OPERATIONS; TRANSPORTING
B01J20/28069
PERFORMING OPERATIONS; TRANSPORTING
B01J20/265
PERFORMING OPERATIONS; TRANSPORTING
B09C1/002
PERFORMING OPERATIONS; TRANSPORTING
B01J20/28045
PERFORMING OPERATIONS; TRANSPORTING
B01J20/3285
PERFORMING OPERATIONS; TRANSPORTING
C02F2103/007
CHEMISTRY; METALLURGY
C02F2209/00
CHEMISTRY; METALLURGY
International classification
B01J20/28
PERFORMING OPERATIONS; TRANSPORTING
B01J20/26
PERFORMING OPERATIONS; TRANSPORTING
Abstract
Methods of passively sampling PFAS in the environment, PFAS sorbents, apparatus and systems (apparatus plus conditions) for sampling groundwater, porewater, and surface water are described.
Claims
1. A PFAS groundwater sampler, comprising: a housing comprising a wall or walls that define an internal cross-sectional area; a PFAS sorbent material disposed within the housing; wherein the sampler has a mass of at least 0.05 grams and a ratio of sorbent mass to housing internal cross-sectional area of no more than 3 g/10 cm.sup.2; and wherein the sorbent has a log K.sub.d of 10 or less for each of PFOA and PFOS and PFBS.
2. The sampler of claim 1 wherein the sorbent is a polymer.
3. A PFAS sampler, comprising: a PFAS sorbent film or foam that is covered by a copper mesh.
4. The PFAS sampler of claim 3 comprising five layers wherein the PFAS sorbent film or foam is sandwiched between two pieces of copper mesh and two pieces of stainless steel mesh such that the sampler comprises layers of the orders: stainless steel:copper:PFAS sorbent:copper:stainless steel.
5. The PFAS groundwater sampler of claim 1 wherein the sampler has a ratio of sorbent mass to housing internal cross-sectional area of no more than 1 g/10 cm.sup.2.
6. The PFAS groundwater sampler of claim 1 wherein the sorbent is a polymeric foam.
7. A PFAS groundwater sampler, comprising: a housing comprising a wall or walls that define an internal cross-sectional area; a PFAS sorbent material disposed within the housing; wherein the sampler has a mass of at least 0.05 grams and a ratio of sorbent mass to housing internal cross-sectional area of no more than 3 g/10 cm.sup.2; wherein the sorbent is a polymeric foam and wherein the foam comprises two types of polyurethane.
8. The PFAS groundwater sampler of claim 7 wherein the two types are ether-polyurethane and ester-polyurethane.
9. A PFAS groundwater sampler, comprising: a housing comprising a wall or walls that define an internal cross-sectional area; a PFAS sorbent material disposed within the housing; wherein the sampler has a mass of at least 0.05 grams and a ratio of sorbent mass to housing internal cross-sectional area of no more than 3 g/10 cm.sup.2; wherein the sorbent is a polymeric foam and wherein the polymeric foam is further characterizable by at least one of the parameters shown in Table 2, 4, or 5 and having a value of ±50% of that parameter as shown in Table 2, 4, or 5.
10. The PFAS groundwater sampler of claim 6 wherein the sorbent is a single material.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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DETAILED DESCRIPTION OF THE INVENTION
(25) Sorbent
(26) Polymers containing carbamate (urethane groups) groups in the main chain are preferred, even more preferred are polymers containing carbamate and ether groups or carbamate and ester groups in the main chain. In a related aspect, the invention includes an open-celled polymer foam comprising PFAS and water, where the polymer containing carbamate and ether groups or carbamate and ester groups in the main chain. We have found that polyurethane foams effectively sorb PFAS in aquatic samples. This is believed due, at least in part, to the interactions between the PFAS and the non-carbon atoms that are part of the polymer main chain. Among polymers tested, we have found that polymers containing both carbamate and ether groups in the main chain are more effective in adsorbing most PFAS analytes, but polymers containing both carbamate and ester groups in the main chain performed slightly better for the problematic short chain analytes which are more soluble and therefore harder to remove through sorption to passive samplers or water treatment substances such as granular activated carbon.
(27) Foam
(28) In some preferred aspects, the invention may use a polymeric, open-celled foam to adsorb PFAS in a passive sampler, and a rigid holder allowing direct placement in the sampled water and an optional transfer of vibrations from a vibrational motor. The preferred sorbent material is polyurethane, especially an open-celled polyurethane foam in which the an organic carbamate moiety [—NH—(C═O)—O— ] linked through an ether or ester linkage. The adsorptive phase is a solid that, due to its surface properties, interacts with PFAS and concentrates them on the solid surface. The polymeric sorbent material (or combination of materials) is suitable for both ionic and neutral PFAS.
(29) The foam preferably has an open pore structure having 200 or less pores per inch (measured linearly along a cross-section), preferably 10-150 or 45 to 100 pores per inch which allows free flow of water though the material. Higher density (more pores per inch) material could be used to increase the surface area of the sampler when needed. Higher surface area would be beneficial for sites with low concentrations of the analytes because it allows to collect more analytes and therefore increase the detection limits. It could be also beneficial at sites where due to the space restrictions that overall dimensions of the passive sampler must be minimized (e.g., in small internal diameter groundwater monitoring wells. The foam material is typically deployed in sheets of material, for example a sheet in the range of 0.1 to 1 inch thick, or 0.1 to 0.5 inch thick, or 0.25 to 1 inch thick.
(30) The foam may alternatively, or in addition, be described by other characteristics. For example, the foam may alternatively, or in addition, be described by its partition coefficient as measured under specified conditions. Other material characteristics of the foam include specific surface area, porosity, acidity and basicity of the material surface, size of the micropores, and zeta potential (a measure of the surface charge).
(31) In the examples section, testing of two types of polyurethane foam are described: an ether-based polyurethane and an ester-based polyurethane. Both types of polyurethane foam (PUF) were obtained from UFP Technologies (see
(32) Prior to use, the foams were cleaned by soaking in methanol three times to remove any contaminants. The volume of methanol used in this step is not critical as it has very high affinity for PFAS and other contaminants, but it is advised to provide enough volume of methanol to allow the foam to move freely during agitation. Up to 5 grams of foam would be appropriate for 250 milliliters of methanol.
(33) An ether-based polyurethane comprises carbamate groups bonded through molecular chains comprising ether moieties. The ether-based polyurethane has a ratio of ether moieties to carbamate moieties of at least one, typically at least 5, preferably at least 10, in some embodiments 2 to 20 or 2 to 10; preferably, carbamate moieties are connected through polyether linkages. Likewise, an ester-based polyurethane comprises carbamate groups bonded through molecular chains comprising ester moieties. The ester-based polyurethane has a ratio of ester moieties to carbamate moieties of at least one, typically at least 5, preferably at least 10, in some embodiments 2 to 20 or 2 to 10; preferably, carbamate moieties are connected through polyester linkages.
(34) Housing/Supports
(35) The housing and/or support for the polymeric foam may be varied depending upon the application site. For example, the polymeric foam may be framed in hinged stainless-steel frames, inserted into a stainless-steel mesh sleeve, or attached to a perforated core. The invention includes devices and methods in which an anti-biofouling screen is placed over (in some embodiments, in direct contact with) a PFAS adsorbent. In preferred embodiments, a polymeric foam adsorbent is sandwiched between anti-biofouling screens. In some embodiments, the anti-biofouling screen is placed directly in contact with the adsorbent, in other embodiments, one or more porous inert layers can be disposed between the adsorbent and the anti-biofouling screen.
(36) A preferred construction for surface water deployment is illustrated in
(37) A device for sampling in a groundwater well is illustrated in
(38) The invention also provides apparatus and methods of acquiring analyte samples that are designed to collect a plurality of samples over a plurality of selected time intervals. A single passive sampler can be placed in a site of PFAS-contaminated water and adsorb PFAS over any selected time period, and a single device can collect multiple samples, each of which is collected over a different, selected time period. To do that, multiple pieces of sorbent (a preferred sorbent is a polymeric foam) are placed inside the hardware, which is equipped with separated compartments for each piece of sorbent and a mechanism that exposes each piece of sorbent one after another. This can be achieved through a variety of mechanisms schematically drawn below. The modes of operation can be generally divided into two groups. The first group are mechanisms that exposed the sorbent for a given time (e.g., three weeks), after which the first piece of sorbent is closed off, effectively capturing the past three weeks of site conditions. After another three weeks, another piece of sorbent is closed off, etc. This can happen either through rotation of the external sleeve or through vertical movement of the sleeve (e.g. Rotary Shutter/Sleeve and Linear Shutter/Sleeve). The second group of methods are methods that after the desired period of time remove/separate the sorbent from the adjacent water, stopping the adsorption. This can be done through removing the sorbent from water (External Winch/Lift or Buoyant Individual Segments) or through lowering an “air bell” into the well (Progressive Dive Bell Sleeve, Stationary Filled Dive Bell).
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(45) In some aspects, the invention provides a passive sampler and a method of sampling comprising: exposing a first piece of sorbent to water at a selected site, closing off the first piece of sorbent, and, at a different time than the first sorbent is exposed, exposing a second piece of sorbent to water at the selected site. The time intervals are not identical and can overlap or not overlap; the second interval preferably starts later than the first. The sorbent is preferably selected to adsorb PFAS. The passive sampler can be automated (typically containing an electronic timing device with actuator) and does not require a human to go to the site to extract and replace a sorbent. In some preferred embodiments, the passive sampler comprises mechanisms that expose the sorbent for a given time (e.g., three weeks), after which the first piece of sorbent is closed off, effectively capturing the past three weeks of site conditions. After another selected time period (e.g., the following three weeks), another piece of sorbent is closed off, etc. This can happen either through rotation of an external sleeve or through vertical movement of the sleeve (e.g. Rotary Shutter/Sleeve and Linear Shutter/Sleeve). In another set of preferred embodiments, after a desired period of time, sorbent is removed/separated the adjacent water, stopping the adsorption. This can be done through removing the sorbent piece from the water (External Winch/Lift or Buoyant Individual Segments) or through lowering an “air bell” into the well (Progressive Dive Bell Sleeve, Stationary Filled Dive Bell). The invention includes any of the passive samplers illustrated in the figures.
(46) The size of the passive sampler can be customized to the site conditions. For surface water deployments, passive sampler can be protected from the particulates with a fine-mesh stainless steel, to protect the sorbent from suspended particulates. Stainless-steel mesh screens with the nominal size (“nominal” meaning the size of particles that can pass through the openings) of 2-100 micrometers are preferred because smaller size mesh may necessitate longer exposure times. The stainless steel provides protection from particulate contamination and physical damage to the sampler during exposure but does not suffer from the same problems typical membranes would cause for PFAS which is adsorption of PFAS to the membrane itself. The sorbent may be also protected from growth of biofouling with a fine-mesh copper screen. The passive sampler can be suspended from a surface buoy or anchored above the sediment. For groundwater, a narrow passive sampler holder will be used such that the sampler fits freely inside the well without restricting the flow. The passive sampler will be lowered into the well using a PFAS-free cable, preferably the cable is stainless steel although polymer (e.g., Nylon) cable may be used if depletion of PFAS within the well is not an issue. The cable can be attached to the outside of the well to hold the passive sampler within the screened interval of the well. The passive sampler will be deployed for a period of time, in some embodiments 2-8 weeks or 2-4 weeks, after which it will be retrieved.
(47) Motor/Vibrator
(48) The sorbent may be connected to a vibrational motor (
(49) Methods of Collection
(50) Preparation:
(51) Prior to deployment, the polymer is cleaned to remove any potential unpolymerized compounds or other contaminants that could interfere with PFAS measurements. This also provides a confidence that no new contaminants will be introduced into the sampled water via passive sampler deployment. Performance reference compounds (PRCs) are sometimes added to other types of passive samplers before deployment to determine if equilibrium was achieved, and if necessary, correct the data for lack of equilibration. Because the PFAS passive sampler was shown to achieve equilibrium in days to weeks (depending on the analyte), the use of PRCs may not be required. However, PRCs could be used in limited flow conditions such as low-permeability porewater where prolonged equilibration times are expected. If PRC use is deemed necessary, polyurethane material can be cleaned as described above, then immersed in an aqueous solution of PRC compounds which display similar properties to the analytes but are absent from the sampling environment. The passive sampler will comprise the polymer adsorbent (optionally spiked with PRCs), stainless-steel parts (frame/canister/mesh), and potentially a laboratory grade membrane, preferably a stainless steel membrane, and an optional copper mesh serving as an anti-biofouling agent.
(52) Deployment:
(53) Generally, from one to any number of samplers can be employed at a site, for example, 3 to 10 samplers. The number may vary, depending on the specific project goals, expected site variability, desired type one and type two errors, and the project budget. Passive sampler should be deployed in so that it is always submerged, which will be of particular concern when sampling near intertidal areas. For surface water, the sampler can be anchored above the sediment or suspended from a buoy or a permanent underwater structure (e.g. a dock). For porewater sampling, the sampler is inserted into the sediment. For groundwater sampling, the sampler is lowered into the well using a cable and positioned within the screened interval, the cable is then fixed to the outside of the well for the time of deployment.
Sample Processing and Analysis:
(54) After retrieval, passive samplers are gently shaken to remove excess water, then packed in Ziploc bags and on ice and sent to the laboratory where they are disassembled to recover the sorbent. The sorbent is then extracted which results in the formation of a solution with significantly higher analyte concentrations compared to the sampled medium, allowing for much lower detection limits compared to standard water analyses (standard analysis methods are USEPA Method 537 and ASTM D7979-16), and analyzed in a laboratory. The concentration of PFAS in the sorbent can then be converted to the concentration of PFAS in the sampled water by using laboratory derived polymer-water partition coefficients.
Examples
(55) The experimental data described below provides sorption characterization data of the used polyurethane foams. The data include: comparison of the initial uptake kinetics in static vs. vibrated system (two analytes); adsorption kinetics in 22-day exposures (15 analytes); adsorption isotherms (15 analytes), the effect of the water parameters on PFAS partitioning investigation, extraction efficiency determination, and field demonstration study results. The analytes targeted in the experiments are listed in Table 1.
(56) TABLE-US-00001 TABLE 1 List of PFAS analytes tested for in examples. Analytes Abbreviation Analyte Full Name CAS No. PFBA Perfluoro-n-butanoic acid 375-22-4 PFHxA Perfluororhexanoic acid 307-24-4 PFHpA Perfluoroheptanoic acid 374-85-9 PFOA Perfluorooctanoic acid 335-67-1 PFNA Perfluorononanoic acid 375-95-1 PFDA Perfluorodecanoic acid 335-76-2 PFUnA Perfluoroundecanoic acid 2058-94-8 PFDoA Perfluorododecanoic acid 307-55-1 PFBS Perflurorbutanesulfonic acid 375-73-5 PFHxS perfluoro-1-hexanesulfonate 3781-99-6 PFOS Perfluorooctanesulfonic acid 1763-23-1 PFDS Perfluoro-1-decanesulfonate 2806-15-7 6:2 FTS 1H,1H,2H,2H-Perfluorooctane sulfonate 27619-97-2 8:2 FTS 1H,1H,2H,2H-Perfluorodecane sulfonate 39108-34-4 N-MeFOSAA N-methylperfluoro-1-octanesulfonamido- 2355-31-9 acetic acid N-EtFOSAA N-ethylperfluoro-1-octanesulfonamido- 2991-50-6 acetic acid
Materials:
(57) All experiments were conducted in high-density polyethylene (HDPE) bottles or polypropylene (PP) tubes. All solvents were HPLC grade. The PFAS analytes were purchased as a neat material or in methanolic solutions from Sigma Aldrich or Wellington Laboratories. All stock solutions were prepared in methanol.
(58) Sorbent Preparation:
(59) The experiments were conducted using the same two types of reticulated PUF as described above. One PUF was ester-based and the other one was ether-based. The PUF was cut to 5 cm×5 cm size for the vibration experiments and to ˜1 cm×1 cm size for all other experiments, then cleaned by three consecutive soaks in HPLC grade methanol with orbital shaker agitation. The first soak was overnight, followed by solvent replacement, 2-hour soak, another solvent replacement and finally 1-hour soak. After that, the solvent was drained and the PUF was dried in the fume hood, then packed in clean HDPE bottle until needed.
(60) Analytical Methods:
(61) All samples were analyzed following serial dilution as per the DoD Quality Systems Manual 5.1 Table B-15 criteria for samples of known high PFAS concentrations using liquid chromatography tandem mass spectrometry (LC-MS/MS) using negative electrospray mode and the analytes quantified using the isotope dilution method.
(62) Effect of Vibration on Uptake Kinetics
(63) To evaluate the effect of vibration on the uptake of PFAS from water, adsorption kinetics of perfluorooctanoic acid (PFOA) and perfluoroactanesulfonic acid (PFOS) were determined in duplicates in vibrated and non-vibrated exposures for both foams. The static experiments were conducted by immersing 5×5 cm pieces of precleaned ester- or ether-based PUF in 500 mL of either PFOS (concentration ˜10 ug/L) or PFOA (concentration ˜5 ug/L) with 0.01 M NaCl as a background electrolyte. For the vibrated experiments the setup was the same except that the foam was attached to a vibrational device consisting of a sonic toothbrush which provided side to side vibration. The solutions in both static and vibrated modes were sampled at 0, 4, 8, 16, 32, and 64 minutes.
(64) The results of the experiment are presented in
(65) Adsorption Kinetics Experiments
(66) Adsorption kinetics experiments were conducted in water solutions of PFAS at concentrations of ˜100 μg/L of each analyte, except for PFDS, N-MeFOSAA and N-EtFOSAA, which were present at concentrations of ˜10 μg/L due to limited amount of the reagents available. The experiments were conducted in triplicates of 125 mL HDPE bottles, with duplicate controls alongside. First, 125 mL of 0.01M NaCl (background electrolyte) in Milli-Q water was added to each bottle. Eight bottles were then spiked with concentrated methanolic stock solutions of the analytes (three bottles for ester-PUF uptake, three bottles for ether-PUF uptake, and two bottles as positive controls (PFAS but no PUF)). With the total spike volume equal of less than 188 μL per bottle, the effect of methanol on the partitioning behavior of PFAS is assumed to be negligible. Negative controls contained 125 mL of 0.01M NaCl and 188 μL of pure methanol; two negative controls contained no PFAS and no PUF, two contained no PFAS but did contain ester-PUF, and two controls contained no PFAS but did contain ether-PUF. The solutions were prepared 1 day before adding PUF and were places on a shaker table to allow for thorough mixing before PUFs were added.
(67) On the first day of the experiment, all solutions were sampled by collecting 500-uL sample (t=0). The experiment time count started when PUF was added. After adding PUF the bottles were placed on the orbital shaker at 130 rpm. The samples (bottles with PFAS and PUF) were sampled after 8 hours, 1 day, 2 days, 6 days, 13 days, and 22 days. The controls were sampled at time 0, 13 days, and 22 days. After experiment termination, the pieces of PUF were air dried and weighed.
(68) Adsorption kinetics varied significantly between analytes and PUF types (
(69) The uptake kinetics were modeled using pseudo-second order kinetic model following the linearization procedures described in Rout et al. (2015):
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where t is the time (d), C.sub.s is the concentration of the analyte in the solid phase (μg/g), k is the kinetic rate constant (g/μg/d), C.sub.e is the concentration of the analyte at equilibrium (μg/g) and ν.sub.0 is the initial sorption rate (μg/g/d).
(71) In addition to, or as an alternative to, any of the descriptions, the sorbents and/or inventive method can be characterized by the kinetic data presented here. For example, the invention can be described as a method (or sorbent) characterizable by one, or any combination, of the values in Tables 2, 4, or 5. This description can be based on ±50%, or ±30%, or ±20% of any of these values. For example, the sorbent, or the sorbent in a method, can be described as characterizable as having a C.sub.e for PFHxA of 59.3±50% (89.0 to 29.6). C.sub.e is measurable by the techniques described herein and in the equation above. This characterization can be in place of, or in addition to, describing a composition of the sorbent. Or a C.sub.e for PFHxA of 59.3±50%, and a C.sub.e for PFOA of 146.7±50%. Or a C.sub.e for PFHxA of 59.3±50%, and a C.sub.e for PFOA of 146.7±50%, and a C.sub.e for PFOS of 411.2±50%. These are merely examples, the invention can be described as characterizable by one, or any combination of the C.sub.e values in Table 2. The above-described characterizations used C.sub.e; however, it should be understood that the method could alternatively be characterized as utilizing a sorbent characterizable by k or ν.sub.o in the equation above.
(72) The ±50% range is selected as reasonably supported by the data in view of the experimental error of the described measurement techniques as well as the ability of workers in this area to modify the sorbent through routine experimentation using the descriptions provided here. The Langmuir-related values for 6:2 FTS, NMeFOSAA, NEtFOSAA, PFDS, PFUnA, and PFDoA are excluded from the characterization of the invention because the uncertainty in these values is too great.
(73) Sorption of all analytes to both types of PUF was well modeled by the pseudo-second order kinetic model except the sorption of 6:2 FTS and PFHxS onto ester PUF, which showed significant scatter of the collected data and therefore increased uncertainty of the obtained results. Modeling results for select analytes are shown in
(74) TABLE-US-00002 TABLE 2 Parameters of the sorption kinetics of PFAS to ether and ester PUFs. Ether PUF Ester PUF C.sub.e k v.sub.0 C.sub.e k v.sub.0 Analytes (μg/g) (g/μg/d) (μg/g/d) (μg/g) (g/μg/d) (μg/g/d) Carboxylates PFHxA 59.3 0.0033 11.7 90.3 0.0249 203.1 PFHpA 120.7 0.0011 16.7 105.2 0.0096 106.0 PFOA 146.7 0.0013 27.2 132.5 0.0127 223.5 PFNA 228.0 0.0025 132.4 183.0 0.0039 129.6 PFDA 366.3 0.0027 368.9 210.6 0.0043 189.0 PFUnA 432.7 0.0068 1270.3 301.7 0.0029 260.8 PFDoA 352.3 0.0260 3230.3 278.9 0.0047 362.7 Sulfonates PFBS 41.0 −0.0104 −17.5 123.0 0.0200 333.6 PFHxS 173.9 0.0012 36.7 150.2 0.0168 378.5 PFOS 411.2 0.0082 1380.1 231.3 0.0192 1025.0 PFDS 52.4 0.7250 1987.5 36.5 0.1274 169.5 Precursors 6:2 FTS 45.7 0.0039 8.1 40.1 0.0022 3.6 8:2 FTS 275.9 0.0028 214.5 147.4 0.0032 70.2 NEtFOSAA 41.9 0.0730 128.1 32.7 0.0320 34.7 NMeFOSAA 48.5 0.0423 99.4 42.0 0.0170 29.5
Extraction Efficiency Determination (PUF Extractions)
(75) Two sets of extraction efficiency experiments were conducted. In the first set (experiment No. 1), extraction of all 15 analytes listed in Table 1 from both types of PUF (ether and ester based) was investigated. First, the two types of PUF were contaminated (loaded) with the analytes of interest. The loading step was conducted by immersing of ester-PUF or ether-PUF in aqueous PFAS solution with analytes concentrations of ˜1000 μL/L (each analyte except PFDS, N-MeFOSAA and N-EtFOSAA which were present at concentrations of ˜50 μg/L each). The solutions were sampled before adding PUF and then again after 8 days of PUF loading on the orbital shaker to determine the initial starting concentration of PFAS on PUF based on the total weight of PUF in each bottle. When loading was completed the PUFs were quickly rinse, dried with paper towels to remove excess water and then placed in the extraction vessels.
(76) Triplicated extractions were conducted for each PUF using five solvents: 0.4% (v/v) ammonia in methanol, 0.4% (v/v) in ethanol, 200 mM NaOH in methanol, 200 mM NaOH in ethanol, and 0.1% (v/v) monoethylamine (MEA) in methanol. Extraction of each sample consisted of three consecutive extraction steps with 4-5 mL of solvent and each extraction step was conducted using 30 minutes of sonication followed by 30-120 minutes of agitation on an orbital shaker. At the end, all three extracts from the same piece of PUF were combined together and analyzed for PFAS concentration and the PUF itself was air dried and weighed to determine the sorbent weight.
(77) The extraction efficiency for each analyte was calculated as the ration between the amount of analyte in the solvent post extraction to the amount of analyte adsorbed to PUF during the initial loading step (i.e., the initial amount of PFAS on PUF before extraction). For some analytes (particularly the shorter chains) very little adsorption was observed during the loading process. If the difference between the final and initial concentration of an analyte in the loading solution was less than 10%, that analyte was excluded from the extraction efficiency cautions to avoid overinterpretation of marginally significant results. The extraction efficiency experiments for these analytes were determine for ether-PUF only in a separate experiment (experiment No. 2) where only the analytes with weaker adsorption were used. This experiment is described below, and the combined extraction efficiency results from the two sets of experiments are presented in Table 3 and discussed in the following paragraph. One important observation from the first extraction experiment was that the ester PUF was broken down by ammonia in methanol and by NaOH in both methanol and ethanol, disabling accurate PUF weight determination post-extraction, so these solvents are not compatible with ester PUF. Ester PUF is therefore preferably extracted with MEA in methanol or ammonia in ethanol. For ether PUF, ammonia in methanol is a preferred solvent because both ammonia and methanol are used in the standard soil extraction methods and therefore are guaranteed not to interfere with the analytical method.
(78) The second extraction efficiency experiment (experiment No. 2) focused on investigation the extraction of the shorter chain (weaker adsorption) analytes only. The goal of this experiment was also to optimize the extraction procedures by determining if certain steps (e.g., sonication) are useful or not. First, a batch of the ether-PUF was contaminated with PFHxA, PFHpA, PFOA, PFNA, PFBS, PFHxS, PFOS, 6:2FTS and 8:2FTS. Spiking solution samples were taken at the beginning and end of spiking to allow calculation of the loading or initial concentration of PFAS in PUF (ng of PFAS per gram of PUF). Unless otherwise noted, the PUF was then retrieved and quickly rinsed with Milli-Q water to remove any unbound analytes and dried off with paper towels. The PUF was then subjected to the following extractions: 0.4% ammonia in methanol with sonication (sonication treatment defined as three consecutive extractions with 5 mL of solvent and 30-45 minutes of sonication followed by 30-120 minutes of agitation on an orbital shaker) 0.4% ammonia in methanol with shaking only (shaking treatment defined as three consecutive extractions with 5 mL of solvent; no sonication, one overnight extraction with agitation on an orbital shaker followed by two shorter extractions [180 and 30 minutes] on an orbital shaker) 0.4% ammonia in ethanol with sonication (as defined above) 0.4% ammonia in ethanol with shaking only (as defined above) Unrinsed PUF (just dried with paper towels) extracted with 0.4% ammonia in methanol with shaking only treatment (as defined above)
(79) After analyzing the extraction solvents, the amount of PFAS desorbed from PUF was compared to the initial loading of PFAS in PUF to calculate the extraction efficiency (expressed in percent). All treatments yielded statistically similar results, and that the extraction efficiencies for most analytes were in the desired range of 100+/−20%. Sonicated ethanol treatment yielded results above 120% for some analytes indicating potential influence of the solvent on the analytical run, so ethanol should be avoided. Rinsing has no significant effect on the results meaning that simply removing majority of the water attached to PUF with a clean paper towel removed most of the unadsorbed PFAS and the rinsing step is not necessary. Both sonicated and shaken only treatments in methanol achieved similar results; for simplicity, shaking only is recommended because it avoid multiple transfers of the sample between sonicator and orbital shaker.
(80) The results are presented in the table below.
(81) TABLE-US-00003 TABLE 3 Extraction efficiencies for all analytes, combined from two sets of experiment described in text. Average extraction Standard Experiment Analyte efficiency (%) deviation No. 2 PFHxA 98 8 No. 2 PFHpA 105 4 No. 2 PFOA 110 6 No. 2 PFNA 95 24 No. 2 PFBS 78 15 No. 2 PFHxS 105 22 No. 2 PFOS 86 21 No. 2 6:2FTS 130 8 No. 2 8:2FTS 83 12 No. 1 PFDA 80 6 No. 1 PFUnA 76 6 No. 1 PFDoA 90 9 No. 1 NMeFOSAA 103 10 No. 1 NEtFOSAA 96 3 No. 1 PFDS 78 3
(82) Adsorption Isotherm Experiments
(83) Adsorption isotherm experiments were conducted to provide sorption characteristics of the chosen polyurethane foams. The experiments were conducted in 125 mL HDPE bottles, which were filled with 125 mL of PFAS solution in 0.01M NaCl (background electrolyte) with varying PFAS concentrations, sampled to determine the starting PFAS concentration, and then a 1 cm×1 cm piece of ester- or -ether PUF was placed in each bottle. The bottles were then closed and placed on an orbital shaker for 21 days.
(84) The starting concentrations of PFAS in the adsorption experiment were 0.05; 0.1; 0.5; 2; 10; 50; and 500 μg/L of each analyte except PFDS, N-MeFOSAA and N-EtFOSAA which were added at approximately 1/10th of these concentrations due to analyte stock amount limitation. Alongside samples, positive controls (2 of 50 μg/L of PFAS but no PUF) and negative controls (no PUF and no PFAS; only ester-PUF; only ether PUF) were prepared. The low concentration bottles (negative controls and concentrations 0.05-2 μg/L) were sampled in through solid phase extraction (SPE) which consumes the sample, so duplicated bottles were prepared for the initial and final concentration measurements. The higher concentration samples were sampled by removing small volume (0.5 mL) of the sample at the experiment initiation and then again at termination; these samples were analyzed using direct injection method. Direct injection samples were preserved with 0.5 mL of methanol and then diluted as needed to fit the range of the method calibrations. All SPE samples were analyzed in duplicates and the direct injection samples were analyzed in triplicates except the two positive controls which were analyzed through direct injection in duplicates. The difference in the initial and final concentrations of PFAS in the tested solutions was used to estimate the amount of the analytes adsorbed to the PUF, which was then converted to ng/g by dividing by the PUF weight determined post-experiment after air-drying. The results were modeled using two adsorption models: Langmuir and Freundlich. Langmuir model following the equation:
(85)
where:
(86) q is the equilibrium amount of analyte on the sorbent (μg/g)
(87) q.sub.max is the sorption capacity of PUF (μg/g)
(88) K.sub.L is the Langmuir adsorption equilibrium constant (L/g)
(89) C is the equilibrium aqueous concentration of analyte (μg/L)
(90) Freundlich model followed the equation:
q=K.sub.FC.sup.n
where:
(91) K.sub.F and n are the Freundlich adsorption constants.
(92) The data were modeled successfully using the abovementioned models for starting water concentrations up to 50 μg/L. The highest starting concentration (500 μg/L) plotted above the isotherms fitted through the remaining data. Such an increase in adsorption at higher concentrations is indicative of a second layer formation (adsorption of the analyte from solution to the analyte already adsorbed to the sorbent), which cannot be described properly with Langmuir or Freundlich isotherms, so this concentration was excluded from the modeling presented below. The example of Langmuir and Freundlich fit to the data for ether and ester PUFs are shown in
(93) TABLE-US-00004 TABLE 4 Adsorption isotherm coefficients for ether- and ether-PUF. Freundlich Freundlich Langmuir K.sub.F Langmuir K.sub.F Carbon K.sub.L q.sub.max (ng/g)/ K.sub.L q.sub.max (ng/g)/ chain L/kg μg/g (μg/L).sup.n n R.sup.2 L/kg μg/g (μg/L).sup.n n R.sup.2 Analyte length Ether PUF Ester PUF Precursors 6:2 FTS 6 0.0014 965,991 930 0.95 0.9531 0.0011 331,927 350 0.89 0.8407 8:2 FTS 8 168 61 5,618 0.80 0.9689 0.0027 557,068 1,299 0.86 0.8303 NMeFOSAA 8 1,506 29 19,684 0.88 0.8848 0.0336 83,303 1,458 0.87 0.8545 NEtFOSAA 8 2,011 36 33,051 0.85 0.8726 0.0067 511,434 2,395 0.92 0.9202 Sulfonates PFBS 4 146 7 525 1.08 0.9421 68 28 626 0.94 0.9390 PFHxS 6 20 135 3,331 0.80 0.9785 194 19 1,139 0.74 0.8299 PFOS 8 271 310 51,852 0.85 0.9865 16 421 8,963 0.81 0.9856 PFDS 10 NA NA 36,937 0.58 0.7638 78 618 29,933 0.84 0.9727 Carboxylates PFHxA 6 230 15 638 0.88 0.8385 333 12 538 0.99 0.8708 PFHpA 7 NA NA 837 0.84 0.8257 139 24 683 0.91 0.8993 PFOA 8 128 22 1,696 0.73 0.8918 200 18 803 0.85 0.8658 PFNA 9 52 110 5,724 0.79 0.9937 163 17 1,159 0.71 0.9443 PFDA 10 134 225 23,026 0.81 0.9948 65 74 2,765 0.70 0.8914 PFUnA 11 141 708 78,352 0.85 0.9877 0.00009 91,529,204 9,189 0.84 0.9831 PFDoA 12 25 14,944 243,232 0.95 0.8883 0.00034 77,371,833 20,368 0.95 0.9767
Distribution (also known as partition) coefficients (K.sub.ds) were also determined for the linear part of the data (lower concentrations). The distribution coefficients provide a scaling factor that allows passive sampler results (C.sub.s, in mass of analyte per gram of passive sampler) to be converted to water concentrations in the sampled water (C.sub.w, in mass of analyte per volume of water), as shown below:
(94)
(95) The distribution coefficient is defined as the ratio of the amount or concentration analyte in/on solid to the amount or concentration of the analyte in liquid, and as such the concept of distribution coefficient only applied to the range of concentrations in which the concentration of the analyte in the sorbent is linearly proportional to the concentration of the analyte in water (the uptake is not concentration depended). For data that follow a non-linear adsorption isotherm (such as Langmuir and Freundlich), the distribution coefficients can be determined from the lower range of concentrations in which the linearity exists. In our data, the linear range was observed for up to 2-10 μg/L of the initial PFAS concentration. The obtained distribution coefficients are summarized in Table 5. It can be seen that the K.sub.d generally increases with the length of the carbon chain. Also, for the same carbon chain length, sulfonate species have higher K.sub.d than carboxylate species. Log K.sub.d values for each of the analyte groups investigated in this study (precursors, sulfonates, and carboxylates) correlate almost linearly with the total number of carbon atoms in the analyte (which for the sulfonates and carboxylates is the same as the length of the main carbon chain) (
(96) TABLE-US-00005 TABLE 5 Distribution coefficients (K.sub.ds) for ether- and ester-based polyurethane foams. Total Main number Log Log carbon of K.sub.d for K.sub.d for K.sub.d for K.sub.d for chain carbon Ether- Ester- Ester- Ether- Analyte length atoms PUF PUF PUF PUF Precursors 6:2 FTS 6 8 1,380 371 3.14 2.57 8:2 FTS 8 10 6,415 1,531 3.81 3.18 NMeFOSAA 8 11 44,716 2,895 4.65 3.46 NEtFOSAA 8 12 80,145 3,531 4.90 3.55 Sulfonates PFBS 4 4 813 1,769 2.91 3.25 PFHxS 6 6 2,277 3,218 3.36 3.51 PFOS 8 8 69,709 5,881 4.84 3.77 PFDS 10 10 NA 48,940 NA 4.69 Carboxylates PFHxA 6 6 2,529 2,750 3.40 3.44 PFHpA 7 7 NA 2,868 NA 3.46 PFOA 8 8 1,355 2,805 3.13 3.45 PFNA 9 9 4,501 2,544 3.65 3.41 PFDA 10 10 25,253 4,340 4.40 3.64 PFUnA 11 11 93,725 8,070 4.97 3.91 PFDoA 12 12 400,567 18,061 5.60 4.26
Effect of Geochemical Factors on K.sub.d
(97) Partitioning between natural waters and various solids for most environmental contaminants is affected by certain geochemical characteristics of the water, which can include pH, ionic strength, total and dissolved organic carbon, temperature, and others. The effect of geochemical factors, including ionic strength and dissolved organic carbon (DOC) concentration was investigated. The experiments were analogous to the adsorption isotherm experiments except that variation of the investigated parameters was added. The experiments were conducted with starting PFAS concentration of 2 (low) and 10 (high) μg/L.
(98) Overall, the data presented in more details below shows that the water parameters can affect partioning of PFAS to the passive sampler, so the basic water measurements could be taken to provide the water concentrations using the pH, DOC, and ionic strength adjusted K.sub.d values. To be determine water concentrations (C.sub.w) in the sampled water after a passive sampler deployment we use the equation: C.sub.w=C.sub.s/K.sub.d; where C.sub.s is the concentration of PFAS in the passive sampler material (PUF).
(99) Ionic Strength
(100) Four ionic strengths were investigated, covering the range of ionic strengths from freshwater to estuarine water. The solutions consisted of 0.1; 0.2, 0.3, and 0.4 M sodium chloride (NaCl). Log K.sub.d values were determined for low and high PFAS treatments for each analyte and ionic strength combination by conducting a one-point regression though the origin on the “amount sorbed vs. amount in solution” (see Langmuir isotherms in
(101) DOC
(102) Four concentrations of DOC were used. The DOC stock solution was prepared from humic acid salt that was mixed with 10 mM monobasic potassium phosphate used as a pH buffer. The mixture was agitated for 24 hours, after which it was centrifuged and then filtered through 0.7 μm glass filter to remove any undissolved particles. So prepared stock solution was used to create working DOC solutions for the experiment. Because the actual humic acid concentration in the humic acid salt neat material may vary, DOC concentration was measured analytically both at the beginning and at the end of the experiment to account for potential DOC loss due to microbial utilization. Starting concentrations of DOC in the four treatments were determined to be 1, 2, 7, and 12 mg/L, which covers a range of typical groundwater and freshwater DOC concentrations, but is lower than typical porewater DOC concentrations. The experiment was prepared both with high (10 μg/L) and low (2 μg/L) starting concentrations of PFAS; however, due to analytical problems only low PFAS concentration data are currently available. The results are shown in the figure below. It can be seen that K.sub.d values vary systematically with DOC concentration, with highest DOC concentration treatments achieving about 0.5-1.0 log unit lower K.sub.d values than in water with no DOC. Further, for carboxylate it is apparent that the relationship between K.sub.d and DOC varies with the PFAS chain length, with the longest chains showing a more even, slight decrease of K.sub.d with increasing DOC, whereas the shortest chain analytes show a more pronounced drop in K.sub.d with low DOC addition but seem to be less affected at high DOC concentrations.
(103) pH
(104) The solutions of varying pH were prepared in MilliQ water with 0.01 M sodium chloride as a background electrolyte. The pH was then adjusted to the desired value by drop by drop additions of 20 mM hydrochloric acid or 20 mM sodium hydroxide while monitoring the pH using a pH meter. Finally, PFAS stock solution was added to the bottles to achieve the starting PFAS concentrations of 2 or 10 ug/L. For each pH and each starting PFAS concentration level, three replicate bottles were prepared (i.e. at pH 4 there were 3 replicates for starting PFAS concentration of 2 ug/L and 3 replicates for starting PFAS concentration of 10 ug/L). Once all the bottles were spiked they were allowed to thoroughly mix on an orbital shaker overnight after which the solutions were sampled (0.5 mL) to determine the time zero concentration of PFAS. A piece of PUF was then added to each bottle and the bottles were placed on the orbital shaker again, where they remained for 23 days to allow equilibration between PUF and the solution. After 23 days, the solutions were sampled again (0.5 mL) and the amount of PFAS on PUF was calculated from the loss of PFAS from solution during the exposure. The PUF was then retrieved and dried to determine its weight so the results can be reported in per gram basis and the solutions were used to determine the final pH through titration. The final pH determination revealed that the pH meter used at experimental setup must have malfunctioned or the solution was not sufficiently mixed before the pH was taken, because the highest pH treatment was about 6 instead of 8. The results cover the range of 4.1 to 6.2. The K.sub.d value was calculated only for analytes that were still detectable in the solution at experiment termination.
(105) The effect of pH on the log K.sub.d values was measured for the starting concentration of PFAS equal to about 2 ug/L (“P=2”) and about 10 ug/L (“P=10”). For PFHxA the pH had no impact on K.sub.d whereas for all the other analytes the log K.sub.d decreases with increasing pH. The strength of the effect does not seem to correlate with the PFAS chain length. The average decrease rate of log K.sub.d with pH for all analytes except PFHxA is value decreases on average by 0.52 log units per 1 pH unit. This relationship can be used to select the correct log K.sub.d to match the pH of the sampled environmental water based on the field pH measurement.
(106) Field Demonstration of the PUF-Based Passive Sampler
(107) A field demonstration study was conducted to determine if the developed passive sampler works in more complicated matrices. Presence of fluctuating PFAS concentrations, changing water temperature and ionic strength, a complex aqueous matrix carrying suspended particulates, organic carbon, and dissolved and adsorbed phase co-contaminants can all affect the performance of passive samplers. In surface water, another potential influence is biofouling on the surface of a passive sampler, which can lower the analyte uptake rate.
(108) The field demonstration was conducted at two airport sites, where due to the firefighting training activities elevated levels of PFAS have been identified. Passive samplers were deployed in both surface waters (small creeks and a small river) and in groundwater monitoring wells, using designs of hardware shown above. The surface water sampler holds a piece of PUF 15 cm×15 cm (225 cm.sup.2); the groundwater sampler can hold up to three pieces 8×13 cm (104 cm.sup.2) each. From laboratory experiments it was determined that about 100 cm.sup.2 should collect a comparable amount of PFAS to a standard 250-mL water sample. To evaluate the performance of the passive samplers, grab water samples were collected for PFAS and total organic carbon (TOC) at each sampling station before deploying the passive sampler and again after retrieving it. Additionally, basic geochemical parameters of the water (pH, temperature, conductivity) were measured in situ by the sampling teams. The passive samplers were deployed for four weeks to allow them to equilibrate with the sorbent. Retrieved passive samplers were packed in Ziploc bags and shipped back to the Battelle's Norwell laboratory while still in the hardware so they could be processed in clean conditions at the laboratory. All passive samplers and water samples were packed on ice for transport.
(109) At the laboratory the passive sampler hardware was disassembled to retrieve the PUF. The PUF was inspected and photographed. Paper towels were used to remove excess water and (where present) sediment particles from the PUF. Because the surface water PUF is twice as large as PUF from the surface water was then split in two; one part was submitted for immediate analysis and the other half was archived or submitted for analysis as a replicate sample. From the groundwater samplers, between one and three pieces of PUF were submitted for immediate analysis.
(110) The water samples were extracted and analyzed for following Battelle's standard operating procedure for non-potable waters. For PUF, a modified solids method was used, following a demonstration of capability study on a laboratory spiked PUF. Water results were reported in ng/L whereas the passive sampler results in ng/g. The weight of the passive samplers was determined post-extraction on air-dried samplers. The passive sampler results (C.sub.s) were used to calculate the water concentrations (Cw-calc) using the below equation:
(111)
(112) The K.sub.d (often reported in its logarithmic form as log K.sub.d) is the solid-water partition coefficient and was determined experimentally for simplified matrix (Milli-Q water and 0.01 M NaCl as a background electrolyte) in batch experiments described in the section called “Adsorption isotherms”. The K.sub.d is analyte and water condition specific, for example it can be affected by water temperature, ionic strength, pH, dissolved organic carbon (DOC), etc. The effect of some of these variables was investigated through laboratory experiments in the section “Effect of Geochemical Factors on K.sub.d” section, which allows correction of the K.sub.d for the effects of the matrix.
(113) To evaluate the performance of the passive sampler in field deployments, the passive sampler-derived water concentrations (Cw-calc) were compared to the average grab water concentration (Cw-grab) calculated as an average between the concentration of PFAS in the water sample collected before deploying and after retrieving the sampler. This analysis was conducted for the analytes for which the partition coefficients were determined in adsorption isotherm section.
(114) When K.sub.d in simplified matrix is used, the Cw-calc account for on average 19% of the Cw-grab in surface water samples (slope of 0.19 and R.sup.2 of 0.86) and 3% in groundwater (slope of 0.026 and R.sup.2 of 0.52;
(115) Because Cw-grab and Cw-calc did not agree very well, the effect of the sampled water matrix was investigated. Analysis of the pH, temperature, ionic strength, and TOC showed that all the parameters except for TOC and, in groundwater, the temperature where similar in the simplified matrix from adsorption isotherm experiments and in the waters tested during the field deployments. The TOC in the field waters was about 7 mg/L on average and because DOC was not measured for these field samples it was assumed that the majority of the organic carbon in these samples is dissolved. Based on the laboratory experiment, 7 mg/L of DOC caused an average of 0.8 decrease in the log K.sub.d value compared to the simplified matrix. When that adjusted K.sub.d was used, the Cw-calc and Cw-grab showed a much better agreement, with surface water Cw-calc values averaging 119% of the Cw-grab values, and the groundwater Cw-calc averaging 16% of the Cw-grab values.
(116) Overall a good agreement between the grab samples and passive sampler derived values was achieved in surface water samples but not in groundwater samples, where the passive sampler data were skewed low compared to water grab samples. It can be noticed that for certain Cw-grab values multiple Cw-calc values exist. These represent field duplicate (FD) samplers (two separate sampling devices deployed within one meter of each other) or splits of the same sampler created by sectioning the PUF from one sampler into two segments (bottom and top). The agreement between select FDs and splits is shown in
(117) We discovered that groundwater monitoring well passive samplers can significantly under-represent the aqueous concentrations of PFAS.
(118) Discussion and Summary of Field Data
(119) While the data observed good agreement between passive sampler and grab water sample results, the two measurements are not directly comparable because: passive samplers measure time-integrated concentrations over the period of deployment while grab samples represent discrete point in time (in this case an average of two time points—deployment and retrieval day); and passive samplers typically only accumulate the freely dissolved fractions of contaminants whereas grab samples also include particle and colloid-bound contaminants. As such, passive sampler derived concentrations are almost always lower than that concentrations measured in bulk water samples. Nonetheless, the passive sampler performed well in surface water samples, with the passive sampler results representing on average 119% of the groundwater grab water sample results when matrix-influence partition coefficients were used in the calculation of PUF data. This highlights the importance of, first, investigating the influence of the matrix on the K.sub.d and then of collecting the necessary water quality and geochemical information (pH, ionic strength, organic carbon) to allow the necessary, site-specific adjustments to the K.sub.d.
(120) The passive sampler results for groundwater samples were significantly lower than the results of grab water sample analysis. First, it is well known that water temperature can affect partitioning of dissolved contaminants onto solids in aquatic systems. The impact of water temperature on PFAS partitioning to PUF (K.sub.d) has not yet been investigated and therefore could not be corrected for. The groundwater temperatures were on the order of 16° C. whereas the surface water temperatures were about 25° C. which is the room temperature at which the K.sub.d values were experimentally determined in the laboratory, so the laboratory-derived K.sub.ds were appropriate for the surface water samples but not as much for groundwater samples. For most environmental contaminants the decrease in temperature causes an increase in K.sub.d; however, several studies suggest that the opposite may be true for PFAS, meaning that the K.sub.d decreases with decreasing temperature. Lower K.sub.d will result in higher calculated water concentrations (see Equation above) and therefore could explain why the passive sampler calculated results are lower than the concentrations measured in grab samples. Another possibility is that the dissolved PFAS exchange between the inside of the groundwater well and the rest of the aquifer was slower than the uptake of PFAS by the passive sampler, in which case the water in the well would become depleted in PFAS and therefore the uptake rate of PFAS by the passive sampler would be lower. That could cause for the passive sampler to not be fully equilibrated during the four-week deployment period, which would cause the passive sampler results to be lower than grab water samples obtained through active pumping. To address this problem, we have designed passive samplers that overcome the problem with PFAS depletion.
(121) To investigate the effect of limited volume of water on the experimentally derived K.sub.d values, experiments of adsorption in batches of the same volume and concentration of PFAS but different size of PUF were conducted. Specifically, a series of bottles with 125 mL of PFAS solution in 0.01M NaCl as background electrolyte were prepared. A full PUF the size of approximately 1×1 cm was then added to three of the bottles, and a piece of half-sized PUF (about 1×0.5 cm) was added to another three bottles. The solutions were sampled at time zero (before adding PUF) and then again after 1, 4, 11, and 27 days. This experiment was conducted for both ether- and ester-based PUF (t-PUF and s-PUF, respectively). The results for select analytes are shown in the