Etiënne L. M. Vermeirssen, Josef Asmin, Beate I. Escher, Jung-Hwan Kwon, Irene Steimen and Juliane Hollender
Eawag, Swiss Federal Institute of Aquatic Science and Technology, 8600, Dübendorf, Switzerland
First published on 29th November 2007
There is an increasing need to monitor concentrations of polar organic contaminants in the aquatic environment. Integrative passive samplers can be used to assess time weighted average aqueous concentrations, provided calibration data are available and sampling rates are known. The sampling rate depends on environmental factors, such as temperature and water flow rate. Here we introduce an apparatus to investigate the sampling properties of passive samplers using river-like flow conditions and ambient environmental matrices: river water and treated sewage effluent. As a model sampler we selected Empore™ SDB-RPS disks in a Chemcatcher housing. The disks were exposed for 1 to 8 days at flow rates between 0.03 and 0.4 m s–1. Samples were analysed using a bioassay for estrogenic activity and by LC-MS-MS target analysis of the pharmaceuticals sulfamethoxazole, carbamazepine and clarithromycin. In order to assess sampling rates of SDB disks, we also measured aqueous concentrations of the pharmaceuticals. Sampling rates increased with increasing flow rate and this relationship was not affected by the environmental matrix. However, SDB disks were only sampling in the integrative mode at low flow rates <0.1 m s–1 and/or for short sampling times. The duration of linear uptake was particularly short for sulfamethoxazole (1 day) and longer for clarithromycin (5 days). At 0.03 m s–1 and 12–14 °C, the sampling rate of SDB disks was 0.09 L day–1 for clarithromycin, 0.14 L day–1 for sulfamethoxazole and 0.25 L day–1 for carbamazepine. The results show that under controlled conditions, SDB disks can be effectively used as passive sampling devices.
Sampling the aquatic environment for pollutants is often a challenging task. Water bodies are rarely well mixed and consequently chemicals are not evenly distributed.5 Concentrations of pollutants often fluctuate and small river catchments can pose additional challenges, as they are often hydrologically very dynamic.6 These circumstances may thwart the use of grab sampling to determine chemical loads. For example, in long term monitoring studies that aim to link exposure to chemicals with effects in organisms, grab sampling is only practicable when concentrations of the target chemicals are fairly stable. In dynamic ecosystems that receive a dynamic input, grab sampling is inadequate. On the other hand, time or flow proportional sampling is very costly. In order to circumvent these difficulties, and to produce a simple, biologically relevant and economical sampling method, passive samplers have been developed.7,8
Passive sampling is described by diffusion processes in, and partitioning between, the aqueous phase and a sampling phase. Under conditions of constant aqueous concentrations, the concentration of a compound in the sampler increases nearly linearly with time, after which the increase flattens and ultimately the concentrations in the water and sampler reach equilibrium.9,10 The main attraction of passive sampling, when employed over the linear uptake phase, is that the technique provides an integrated measure of the presence of chemicals at a sampling site. A major drawback of the method, is that it is not straightforward to calculate time weighted average concentrations from passive sampling data. The main reason for this is that the diffusion and partitioning processes are influenced by temperature, turbulence around the passive sampler/water interface and fouling of the sampler.11–13
A major part of our work deals with polar organic contaminants that occur in rivers and various stages within the sewage treatment process. The present study focuses on two aspects that are important in driving the passive sampling process in these aquatic systems: flow regime and matrix (i.e. river water and treated sewage effluent). To our knowledge, the interaction between these two parameters has not been investigated yet. One previous study looked at the effect of turbulence (fluid stirring rate) on the sampling rate of a passive sampler for polar compounds.14 Alvarez and co-workers14 showed that a change from “not stirring” the sampled water to “stirring” leads to an increase in sampling rate of four- to nine-fold (depending on the substance). More such studies exist for samplers for non-polar compounds. For example, Vrana et al.15 looked at the effect of flow rate on the sampling rates of semi permeable membrane devices (SPMDs). However, flow rates in their study were very low, only up to 14 mm s–1, and consequently not comparable with conditions in rivers and wastewater treatment plants. Using Empore™ C18 disks saturated with octanol, also targeting hydrophobic substances, Vrana et al.16 investigated the effect of water turbulence on the passive sampling process. All three studies14–16 used controlled media-tap water spiked with chemicals—and not environmental matrices.
Here, we monitored the performance of a passive sampler for polar compounds under controlled, yet very close to environmental, conditions. To achieve this, we constructed two simple and robust channel systems that were fed with either river water containing treated sewage effluent or undiluted effluent. The design of this new system is described in detail together with first applications. We collected 24 h composite water samples to link aqueous concentrations with passive sampling data and to provide information on field sampling rates. The main question was how environmentally relevant flow regimes and matrices affect sampler performance. To evaluate if the samplers were operating in the integrative mode, we exposed the samplers sequentially and concomitantly for 1 to 8 days.
As a passive sampler model to test in our channel systems, we selected Empore™ SDB-RPS (poly(styrenedivinylbenzene) copolymer, modified with sulfonic acid groups), for several reasons. First, polar compounds can effectively be sampled by the receiving phase when used without a diffusion limiting membrane17,18 (own unpublished work). Second, SDB disks were shown to be operating in an integrative sampling mode for at least 5 days in a lab study18 and a field trial.19 Third, recently a streamlined polycarbonate Empore™ disk holder, i.e. Chemcatcher body, has become available that suits the deployment of these disks in our experimental system.20
With respect to the analyses of samples, we focused on environmental estrogens using a receptor based bioassay (the yeast estrogen screen, YES).21 In addition, we selected three pharmaceuticals with different substance properties that were measured using LC-MS-MS: a macrolide (clarithromycin) and a sulfonamide antibiotic (sulfamethoxazole), as well as an anticonvulsant/analgesic (carbamazepine).
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Fig. 1 Channel system to investigate the effect of flow rate on the sampling performance of passive sampling devices. |
The dispenser box was dimensioned in such a way that there was always some overflow. Thus, the hydraulic head at the holes of the vents remained constant (0.30 m). Surplus water could leave the dispenser box via a large slit, the overflowing water also drained into the basin.
The water in the basin was continuously refreshed at a rate of approximately 1.9 L s–1. Mixing in the system was such that more than 95% of the water was renewed within 10 min. We assessed this by letting the system run without refreshing for a couple of hours. This caused the water temperature to increase, as heat produced by the pump was transferred to the water. Using a temperature logger, we then monitored how quickly the ambient temperature was reached after refreshing was started.
To plan the size of the holes in the caps on the vents, we ran a series of preliminary tests. We tested four hole sizes and we measured the volume of water that was discharged through a hole of a given size. There was a linear relationship between the area of the hole and the amount of water discharged through the hole. The following diameters were selected for the trials: 12, 17, 27 and 46 mm. They corresponded to the following volumetric flow rates: 0.26, 0.55, 1.5 and 3.7 L s–1. Given a water depth in the channels of 0.1 m, this produced flow rates of: 0.026, 0.055, 0.15 and 0.37 m s–1. We checked the accuracy of this calculation in two ways: (1) by simply measuring the flow with a flow meter (MiniAir2, Schiltknecht, Gossau, Switzerland), and (2) by measuring the time for small particles to travel a distance of 0.5 m. These measurements agreed well with the calculated velocities.
One channel system was placed at the Eawag, Dübendorf (Switzerland) and was run with water from the river Chriesbach, which flows through the site. This river contains treated sewage effluent from the sewage treatment works (STW) Bassersdorf, located 6 km upstream. The other channel system was placed at STW Wüeri in Regensdorf (Switzerland) and used effluent that was taken just after sand filtration. During experiments, river water and effluent temperatures were logged inside the channels (Hobo Pendant; Bakrona, Zürich, Switzerland). Experiments were run in the dark, and no visible fouling was observed (see ESI for photos†).
Typical values of general water parameters for the Chriesbach are: pH, 8.0; and conductivity 600–700 µSi cm–1. For sand filtered effluent at STW Wüeri these values are: pH, 7.7; and conductivity, 800–900 µSi cm–1.
A Chemcatcher body has three holes in its rim. Using these holes, two samplers (i.e. duplicates) were fastened onto an aluminium sheet using cable ties. The aluminium sheet was suspended into the water from the top of the channels so that it was parallel to the water flow.
After the exposure period, the SDB disks were rolled up and transferred to a 8.5 mL vial filled with 7 mL of acetone. The vials were transported to the lab and sonicated for 5 min. Subsequently, the acetone was transferred to a new vial and the SDB disk sonicated again, this time with 7 mL methanol. The methanol was added to the acetone and the combined solvents were filtered through a 0.47 µm PTFE membrane in a polypropylene housing (Sartorius AG, Göttingen, Germany), evaporated under a stream of nitrogen to ca. 100 µL and taken up to 500 µL with methanol. The extract was divided in two parts, 100 µL was used for biological analysis, the remainder for chemical analysis.
During Trial II (starting on January 21, 2007), additional sets of SDB disks were placed in the four channels with effluent. These disks were exchanged each day; again, to address the issue of integrative (or equilibrium) sampling. In the second trial we also took 24 h composite samples (100 mL every 20 min) in parallel to the 24 h SDB disk exposures (see Table 1 for further details of the sampling regimes).
Flow speed/m s–1 | Effluent | River water | ||
---|---|---|---|---|
a Every 20 min, 100 mL of water was pumped from the collection basin and pooled to obtain a 24 h composite effluent sample on each of 5 days. | ||||
Trial I | ||||
0.026 | 0–5 d | 0–8 d | ||
0.055 | 0–5 d | 0–8 d | ||
0.15 | 0–5 d | 0–2 and 3–5 d | 0–8 d | 0–4 and 5–8 d |
0.37 | 0–5 d | 0–8 d | ||
Trial II | ||||
0.026 | 0–5 d | 5 times 1 da | 0–8 d | |
0.055 | 0–5 d | 5 times 1 da | 0–8 d | |
0.15 | 0–5 d | 5 times 1 da | 0–8 d | |
0.37 | 0–5 d | 5 times 1 da | 0–8 d |
MS-MS detection (API 4000; Applied Biosystems, Ontario, Canada) was performed in the selected reaction mode (SRM), with positive electrospray ionisation using a source voltage of 5 kV, and an ion transfer capillary temperature of 390 °C. The monitored transitions of the pharmaceuticals and their internal standards are reported elsewhere22 (transition of carbamazepine; 237.1 to 194.2 (quantifier), 237.1 to 192.1 (qualifier); see Table 2 for further details of the analysed compounds). Limits of quantitation for sulfamethoxazole, carbamazepine and clarithromycin were: 9, 2 and 4 ng L–1 for SPE samples and 3, 11 and 1 ng per SDB disk (based on a signal-to-noise ratio >10). The amounts of the analytes per SDB disk were corrected based on the recoveries of the internal standards in each sample.
Compound | Therapeutic class | CAS | Chemical structure | Molecular weight | pKa34 | LogKOW |
---|---|---|---|---|---|---|
Sulfamethoxazole | Sulfonamide- antibiotic | 723-46-6 | ![]() | 253 | 1.8 5.7 | 0.89 |
Carbamazepine | Anticonvulsant/analgesic | 298-46-4 | ![]() | 236 | <1 13.9 | 2.45 |
Clarithromycin | Macrolide-antibiotic | 81103-11-9 | ![]() | 748 | 8.9 | 3.16 |
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Fig. 2 The association between water flow rate and the estrogenic activity (EEQ) on SDB disks exposed to effluent (left Y-axes) and river water (right Y-axes). Data from Trial I are shown on the left and data from Trial II in the middle. The right panel shows the comparison between a 5 day sampling block (repeated from the middle panel and divided by 5 to get a daily average value; diamonds) and the average of five subsequent 24 h samplings (squares). Data were fitted with eqn (2) (lines). |
In Trial I, the plot of EEQ against flow rate flattened off sooner for effluent than for river water. In Trial II the EEQ plots were more similar, though again, at higher flow rates, the relationship remained steeper for river water compared to effluent. One has to note, however, that there were two different sampling times, thus a direct comparison is not possible.
The average daily EEQs sampled (ng per SDB disk) were between 44% (at 0.055 m s–1) and 66% (at 0.37 m s–1) higher for the daily SDB samples compared to the disks that sampled the full 5 day period (indicating that the integrative sampling phase was exceeded).
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Fig. 3 The association between water flow rate and the amounts of three pharmaceuticals on SDB disks exposed for 5 days in effluent (left Y-axes) and 8 days in river water (right Y-axes). Top panels, data from Trial I; lower panels, data from Trial II. Data were fitted with eqn (2) (lines). |
Fig. 4 shows that the SDBs that were changed on a daily basis collected more pharmaceuticals compared to the disks that were left for the full 5 day period. The discrepancy was largest for sulfamethoxazole, from 72% at 0.026 m s–1 to 250% at 0.37 m s–1; intermediate for carbamazepine, from 47% to 227%; and smallest for clarithromycin, from 7% to 53% (indicating that, at the lower flow rates, clarithromycin was sampled in a nearly integrative mode).
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Fig. 4 Daily average amounts of three pharmaceuticals sampled by SDB disks over a 5 day sampling window (diamonds) and over the five subsequent 1 day samplings that comprise the 5 day window (squares). The data were fitted with eqn (2) (lines). |
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Fig. 5 Left: concentrations of pharmaceuticals in five 24 h composite samples of treated sewage effluent. Right: concentrations of the pharmaceuticals in 24 h composite samples offset against the amount of each pharmaceutical adsorbed onto SDB disks over the corresponding 24 h period. The data were fitted with linear regressions (eqn (3)).‡ |
When the daily concentrations of a substance varied over the 5 day period, these concentrations tended to correlate with the amounts of that substance found on SDB disks exposed at 0.026 m s–1 over the same 24 h period (Fig. 5). These data were fitted with linear regression lines (with the intercept set to zero) to get an approximation of the apparent sampling rates RS.
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The pharmaceutical concentrations in the effluent (Trial II) were in line with what has previously been reported.22,25 Considerably higher amounts of pharmaceuticals were sampled by SBD disks in Trial II compared to Trial I. This difference between the two trials may reflect the increased use of pharmaceuticals, especially antibiotics, during the winter.25 Additionally, changes in the efficiency of the treatment process can affect the load of pharmaceuticals in the effluent.22,25,26
Compared to the effluent, between four to 12-fold lower amounts of pharmaceuticals were sampled per SDB disk from river water. This result can be expected, as the river contains effluent that is considerably diluted. It is intriguing, however, that in both trials, a higher estrogenicity was found in river water compared to the effluent. This contrasts with the data on the pharmaceuticals and may point to an unknown emission of estrogens into the river, or a particularly poor estrogen removal rate at STW Bassersdorf, the STW that discharges into the river Chriesbach.
The biological results show a slightly different picture, however. This may be explained by the fact that the estrogenicity data incorporate the effect of a mixture of compounds that react with the human estrogen receptor. In addition, the bioassay is susceptible to matrix components that modify the results.27 Therefore, if the estrogenic cocktail differs over time or between the matrices, different relationships can be expected. As the various components of the cocktail are likely to differ in their relationship between flow rate and sampled amounts—analogous to the differences observed between individual pharmaceuticals. Therefore, it is important to consider that bioassay results are much less amenable to modelling than single compounds, particularly when bioassay results depend on mixtures of (unknown) compounds with differing chemical properties.
In our figures we illustrate the relationship between flow rate and sampled amounts with an empirical model (eqn (2)). If the sampling rate is dominated by aqueous boundary layer diffusion under a laminar flow regime, an increase flow rate (v) should lead to an increase in the sampling rate according to v0.5, as previously stated. The average value for the parameter “c” (in vc) was 0.7, which is slightly higher than the theoretical value. This implies that the effect of flow rate on the overall exchange rate is more significant for the “real” sampler than for an “ideal” flat sampler. Although the Chemcatcher body is streamlined, there is a rim around the SDB disk that may affect the flow conditions over the SDB disk. Increased flow rates will increase the intensity of turbulent eddies near the rim and will eventually increase the overall transfer rate more than expected by the theoretical laminar flow assumption. Moreover, fitting the empirical model to the four experimental data points results in only one degree of freedom. Consequently, any quantitative interpretation of the fitted parameters is not possible.
In Trial I, the temperatures matched our expectations. However, data from Trial I indicated that the sampling window of 5 or 8 days was too long. At a flow of 0.15 m s–1 we compared the amount sampled over a 5 or 8 day sampling window (effluent and river water, respectively) with the sum of the amounts sampled in two sampling slots within these windows (see Experimental section for details). For sulfamethoxazole and carbamazepine, the sum of the two slots exceeded the amounts sampled over 5 or 8 days (data not shown). To address the issue of the length of the integrative sampling phase in more detail, we included a daily sequential sampling protocol for all four effluent channels in Trial II. It emerged that the daily average amount sampled per SDB disk in the 5 day sampling window was below the average of the 5 individual days for most compounds and most flow rates (Fig. 4). For example, at 0.026 m s–1, the daily average amount of clarithromycin sampled over 5 days agreed well with the average amount sampled on the five subsequent days with a difference of 7%. At higher flow rates, up to 35% less clarithromycin was sampled over 5 days compared to the sum of the 24 h sampling periods. Thus, the samplers were in the integrative uptake mode at the lowest flow rate but not at higher flow rates. While for clarithromycin the sampling mode was integrative at 0.026 m s–1, sulfamethoxazole never showed agreement between the average of the five 24 h sampling periods and the average daily amounts calculated for the 5 day period. In fact, the samplers exposed for 5 days collected similar amounts of sulfamethoxazole between 0.055 and 0.37 m s–1. This indicates that equilibrium was reached under these conditions, corresponding to 116 ng of sulfamethoxazole per SDB disk.
It is generally assumed that passive samplers are integrative to up to 50% of the equilibrium.9 For sulfamethoxazole, the maximum for the 24 h samples was 58 ng SDB–1, this is exactly 50% of the equilibrium amount after 5 days. Consequently, the 24 h sulfamethoxazole data meet the criterion for an integrative sampling window. For carbamazepine, all 24 h sampler data (maximum: 840 ng SDB–1) were below 50% of equilibrium amount (>1900 ng SDB–1), also indicating an integrative uptake mode. This is also the case for clarithromycin. Moreover, the sampled amount of clarithromycin over 5 days at 0.026 m s–1 was only 620 ng SDB–1, well below 25% of the equilibrium amount (>2500 ng SDB–1). This indicates that clarithromycin should have been in the linear uptake phase over 5 days at this flow rate. This assumption is supported by the fact that, at the lower flow rates, the data for the 24 h samplings and the 5 day sampling window matched rather well (Fig. 4).
As expected, there is a direct relationship between the hydrophobicity of the compounds, expressed as octanol–water partition coefficient KOW, and the uptake kinetics. Sulfamethoxazole, with its low logKOW (0.89),28 reaches equilibrium fast, while the most hydrophobic compound of our test set, chlarithromycin (logKOW 3.16),29 remains in the integrative phase longest. Carbamazepine has an intermediate logKOW (2.45)30 and shows an intermediate uptake kinetic. This situation is analogous to samplers for more non-polar compounds, where the time to equilibrium increases with the KOW of the sampled substance.9,31
Overall, we can conclude that the investigated compounds were sampled in an integrative manner over 24 h. For a longer exposure period, integrative sampling cannot be assured, especially at high flow rates and for compounds of low hydrophobicity. The integrative sampling window in our experiments is shorter compared to previous studies.17–19 This may be explained by the fact that we used newly developed and streamlined Chemcatcher bodies.20 In the older design, the Empore™ disk is surrounded by a 20 mm deep Teflon rim; this slows down sampling rates.32 Obviously, slower sampling rates provide for a longer integrative sampling window. Should longer integrative sampling periods be required, diffusion-limiting membranes can be used to slow down sampling rates.17,20,33
What needs to be addressed in future studies is whether identical sampling rates can be achieved in different matrices (different rivers and different effluents). This would involve collecting multiple SDB disk and SPE combinations at a large number of sites.
The shape of the relationship between flow rate and sampled amounts is highly repeatable over time for individual pharmaceuticals. Furthermore, this relationship appears to be unaffected by the two matrices that we tested in our trials (i.e. treated sewage effluent and river water containing effluent). Given this reproducibility and the good association between aqueous concentrations and accumulated pharmaceuticals on SDB disks, our data show that SDB disks can be used as passive samplers in the integrative mode, but only when a low flow rate can be maintained at a fairly constant level. The prospect of using SDB disks as equilibrium samplers for selected—fast responding—compounds or under conditions of high flow-rate is an interesting topic that requires more study.
Footnotes |
† Electronic supplementary information (ESI) available: Photos of channel system and temperature profiles of treated sewage effluent and river water. See DOI: 10.1039/b710790k |
‡ For clarithromycin we had to reanalyse the samples after storage. We observed a significant reduction of the values for both the SDB disks and the water samples, which may be explained by the use of oleandomycine as the surrogate internal standard (see Experimental section for details). Results of aqueous concentrations and SDB disks were similarly affected. |
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