1. Introduction
Pharmaceuticals belong to emerging organic contaminants and have recently been the focus of research due to their high frequency of detection in the environment [
1]. The behavior of pharmaceuticals in water systems is ruled by complex processes, which remain poorly understood, particularly in groundwater [
2,
3,
4,
5]. The fate and transport of pharmaceuticals in groundwater as well as risks of possible groundwater contamination are therefore difficult to predict.
Improving the understanding of pharmaceuticals’ transport in heterogeneous and dynamic hydrogeological settings requires the knowledge of crucial processes and transport parameters, which are, however, difficult to determine at complex field sites. For instance, as noticed by Meckenstock et al. (2015) [
6], the true drivers controlling the degradation of low level contaminants are not yet understood well. Concerning mass transfer processes, the heterogeneity of the sediment is often overlooked, which corresponds to ignoring the effect of different flow velocities on the fate of contaminants. Reducing the complexity at field sites, laboratory experiments in column studies can help to identify the specific sorption and biodegradation rates of pharmaceuticals.
Column experiments are frequently used to study the transport of contaminants like micropollutants, such as pharmaceuticals [
7]. Numerous studies have proven the usefulness of column experiments, as they are relatively fast, uncomplicated to manage, and their boundary conditions can be easily controlled. Moreover, different scenarios may be simulated, for example, managed aquifer recharge [
8], seepage through the vadose zone [
9], transport through an aquifer [
10,
11], and bank filtration [
12,
13,
14].
Column studies have been utilized to study the influence of physico-chemical conditions within an aquifer on pharmaceutical transport, with an emphasis on changes in pH [
11], redox conditions [
13,
15], or temperature [
16]. Also, the influence of the sediment type on transport behavior was studied and the following properties were found particularly crucial: Sediment grain size [
17], available mineral surfaces [
18], or total organic carbon content [
19]. However, little is known on the impact of flow velocity on pharmaceutical transport in groundwater [
20].
The effect of pore-water velocity on contaminant transport has been presented in the literature, especially in the context of sorption/desorption studies [
21,
22,
23], but also in degradation studies [
24]. Increased flow velocity may increase biodegradation, if transport and not microbial degradation is limiting the scale of pore-water velocity. On the contrary, if diffusion becomes the dominant mode of substrate transport, as most microorganisms are attached to sediment particles, increased flow velocity may lead to decreased biodegradation [
6]. For example, Mendoza-Sanchez et al. (2010) [
25] found that at higher flow velocity, the degradation of cis-DCE was more efficient than at lower velocity. They explained this fact by the lower flux of the electron donor (yeast extract) enabling sustained dechlorination. Thus, at the field scale, the heterogeneity of the flow velocity may be a controlling factor of for the biodegradation of contaminants. According to Langner et al. (1998) [
26], degradation of 2,4-dichlorophenoxyacetic acid is independent of the retention time but increases with decreasing flow velocity. This can be explained by several processes, which may occur individually or simultaneously, as the resulting effect of pore-water velocity on: (i) Distribution of biomass, (ii) nutrient concentration, (iii) residence time, and (iv) solute mass transfer. Syngouna and Chrysikopoulos (2012) [
27] found that the flow velocity did not influence the transport of biocolloids (waterborne fecal indicator organisms). Similarly, Hendry et al. (1999) [
28] stated that the transport of bacteria was not affected by flow velocities, and similar retardation factors were found for a range of different flow velocities. In the study of Pang et al. (2002) [
23], in which nonequilibrium transport of Cd, Zn, and Pb in gravel columns was examined, the pore-water velocity was found to be positively correlated with the partitioning coefficient, β, forward rate, and backward rate, and negatively correlated with the retardation factor, R, and mass transfer coefficient, ω. Grösbacher et al. (2018) [
24] studied toluene biodegradation in a flow-through system and observed a decrease in the maximum specific growth rate of microorganisms with increasing flow velocity. Teijón et al. (2014) [
20] investigated naproxen transport in columns filled with sandy aquifer material and found no significant influence of the flow velocity on sorption. The obtained residence times were insufficient to see any possible effect with higher pore water velocities.
Besides the properties of the compound itself, transport mechanisms are dependent on the properties of the sorbate and also the properties of the groundwater [
7]. Concerning the sorbate grain size, the area of the surfaces was also found to play an important role. Greenhagen et al. (2014) [
17] compared the sorption and biodegradation of methamphetamine, acetaminophen, and caffeine in columns filled with sand and fine-grained sediment. The removal of the compounds due to degradation and sorption was lower in the sandy column. Further, the total organic carbon content and pH were found to influence the transport of pharmaceuticals in groundwater [
19].
The physico-chemical conditions in the aquifers strongly influence the sorption of pharmaceuticals. Many environmentally relevant pharmaceuticals contain dissociable functional groups and are in dissociation equilibrium, which depends on pH. Therefore, significant pH dependence on sorption was observed for those compounds [
11]. Also, redox conditions are reported to be crucial for contaminant removal from groundwater and soil [
13,
15]. For instance, sulfamethoxazole transformation depends strongly on nitrate-reducing redox conditions [
29]. Moreover, the temperature may influence the biodegradation of pharmaceuticals [
16,
30].
The aim of this study was to investigate the transport behavior of selected pharmaceuticals under different flow velocities and in different sediments. The analyzed substances included: Antipyrine (other name: phenazone), atenolol, carbamazepine, caffeine, diclofenac, ketoprofen, and sulfamethoxazole. The results of this work, especially the transport parameters quantified using an analytical transport model, advance the understanding of pharmaceuticals’ transport in groundwater.
2. Materials and Methods
2.1. Chemicals, Sediment, and Groundwater
The sediment and groundwater, as well as the chemicals used in the experiment, were analogous to those described in Kiecak et al. (2019) [
31] (please note, sediment E from this study was described in the previous paper as E3). The sediment was either purchased (sediment G—coarse technical sand) or collected in two distinct field sites: Sediment V (sandy loam) in the Vistrenque alluvial aquifer in France [
32,
33] and sediment E (medium sand) in the Baix Fluvià fluvio-deltaic aquifer in Spain [
34,
35].
Table 1 gives an overview of the sediment and water properties. Prior to use in the experiments, the sediments were air-dried, homogenized, and sieved to remove individual larger parts (>2 mm).
2.2. Experimental Set-Up
The experiments were carried out using stainless steel columns equipped with steel and silicon tubes to minimize the sorption of chemicals to the used material. The columns were packed stepwise with sediment and saturated from the bottom.
Column experiments were performed in saturated conditions using a peristaltic pump (Minipuls 3, Gilson, Inc., Middleton, WI, USA) to provide a constant water flow from the bottom to the top. Water samples were collected at the outflow using fraction collector (Model LF10 5M, Ma Ron GmbH, Germany) while sampling intervals were adjusted depending on the flow rate. The columns used for the G- and E-experiments had a length of L = 50 cm, and an inner diameter of φ = 9 cm. the columns for the V-experiments had the same length and a diameter of φ = 5 cm. A schematic figure showing the experimental set-up can be found in the
Supplementary Material (Figure S1).
The columns were flushed with “natural” groundwater (brought from the respective field sites) for a few weeks until hydrochemical equilibrium between water and sediment was assumed to be reached. Each experiment was performed in a biotic column (B) and an abiotic control column (A) to distinguish between biological and chemical degradation. Both columns were prepared in the same manner. However, to ensure abiotic conditions, sodium azide (NaN3) was added to the supplying water tank for the abiotic column experiments (final concentration of ca. 0.05 g/L).
Experiments were conducted as flow-through experiments under saturated conditions, with the inlet at the bottom and the outlet at the top of the column. Different flow rates, adapted to the sediment type and mimicking the possible real-world-conditions, were tested for each column, starting with the fastest flow rate (
Table 2). By changing the flow rates, different pore water velocities and transit times were established, and the influence of different residence times in the biotic and abiotic column on the transport behavior of the pharmaceuticals was analyzed. Due to the small difference in the porosity of the two columns (A and B), the achieved velocities were slightly different.
The compounds were first dissolved in methanol (except of caffeine, well soluble in water), a concentrated mix solution was made, and an aliquot of it was then mixed with respective water. At the start of every experiment, a pulse (1.5–2 pore volumes) of tracer solution containing pharmaceuticals (ca. 100 µg/L) and the conservative tracer bromide was applied. The length of the injection was variable and adjusted to the flow rate. The outflowing water was collected into glass tubes using a fraction collector placed in a specially made container (dark, low temperature, e.g., to prevent concentration loss due to photolysis). Sample volumes were about 15 mL. Only selected samples were analyzed because of the high temporal resolution of the sampling. The experiments were operated at room temperature (21 °C).
After each experiment, the columns were flushed again with clean water prior to starting the next experiment with a lower flow velocity. To ensure that none of the studied compounds were still present in the outflowing water, samples were taken and analyzed with LC-MS/MS (results not shown).
2.3. Quantification
Concentrations of pharmaceuticals were measured with an LC-MS/MS system consisting of an Agilent 1200 binary pump (Agilent Technologies, Böblingen, Germany) and a mass spectrometer AB Sciex API 2000 Q-TRAP (Applied Biosystems, Framingham, MA, USA). A Kinetex C18 column (2.6 µm 100 Å, 150 × 3 mm; Phenomenex, Aschaffenburg, Germany) was used. The details on the method were the same as those presented in [
31].
Major ions were measured with ionic chromatography (bromide in the G-experiment in Dionex 500, Dionex, Sunnvale, CA, USA; major ions in the remaining experiments in Dionex ICS-1100, Dionex, Sunnvale, CA, USA). Among the major ions, nitrate was analyzed and served as an indicator of the redox conditions in the columns.
Dissolved oxygen concentrations were measured using flow-through cells (FTC-SUPST3-US PreSens, Regensburg, Germany) at the outlet of each column. Dissolved oxygen was monitored continuously in the biotic columns and occasionally in the abiotic columns. In the abiotic columns, the oxygen concentration remained stable during all experiments, therefore more frequent monitoring was unnecessary.
2.4. Transport Modelling
The results were modelled using the STANMOD software in the CXTFIT 2.1 code [
36]. CXTFIT 2.1 is based on the one-dimensional convection-dispersion equation (CDE). The program provides options for direct and inverse modelling. The inverse modelling can be done for different types of models, including the deterministic equilibrium CDE and the deterministic non-equilibrium CDE. Therefore, the objective function, which is a build-up of the squared differences of observed and fitted concentrations, is minimized by a nonlinear least-squares inversion procedure [
37]. First, the observed concentrations of bromide were analyzed; the fitting parameters included the pore-water velocity,
vp, and dispersion coefficient,
D. For bromide, the retardation factors,
R, and degradation rates,
μ, were assumed to equal 1 and 0, respectively. In the next step,
vp and
D were assumed to stay constant, but
R and
μ were modelled for each of the reactive tracers.
Other parameters were calculated using the following formulae:
where
α—dispersivity [L],
L—column length [L],
neff—effective porosity [-],
Q—discharge [L
3T
−1],
A—cross section area of the column [L
2], and
t0—mean transit time [T].
2.5. Interpretation
Observed concentrations, C, were normalized to the initial concentration, C0, thereby enabling a comparison of the breakthrough curves. Time was also normalized to the mean transit time, t0, which can be a simplification related to the pore volume.
A comparison of degradation rates for biotic and abiotic conditions allows a rough estimation of the biodegradation rates. It was assumed that the degradation in abiotic columns is related to chemical processes, whereas in the biotic column, it is a sum of chemical and biological processes. If, in the biotic column, the degradation rate is higher than in the abiotic column, it is an indicator of ongoing biological processes.
The sorption coefficient,
Kd, can be approximately calculated based on the retardation factor,
R, using the formula:
where
neff—effective porosity [-], and
ρ—bulk density [ML
−3].