|
|
||||||||
í
im
nekb
a Dep. of Soil Science, North Dakota State Univ., Fargo, ND 58105
b Dep. of Environ. Sciences, Univ. of California, Riverside, CA 92521
c Dep. of Biosystems Eng. and Environ. Sciences, Univ. of Tennessee, Knoxville, TN 379964531
d Animal Metabolism: Agricultural Chemicals Research, Biosciences Research Lab., USDA-ARS, Fargo, ND 58105-5674
* Corresponding author (francis.casey{at}ndsu.edu)
Received for publication July 26, 2004.
| ABSTRACT |
|---|
|
|
|---|
Abbreviations: ASE, accelerated solvent extractor CI, confidence interval LCMS, liquid chromatography/mass spectrometer SSQ, sum-of-squares error TLC, thin-layer chromatography
| INTRODUCTION |
|---|
|
|
|---|
Recent batch (Lee et al., 2003) and column studies (Das et al., 2004; Casey et al., 2003, 2004) have found that hormones have short half-lives and a high affinity for sorption in natural soils. However, definitive mechanisms of hormone sorption and transformation in soil are still not fully understood. A better understanding of these mechanisms and their interaction is necessary for explaining why these hormones are consistently detected in natural aquatic systems (e.g., Kolpin et al., 2002; Gentili et al., 2002; Kuch and Ballschmitter, 2001), albeit in small concentrations. The objective of this research was to improve the understanding of the processes of sorption, mobility, and transformation for estrogens in natural soils, and their interaction, using improved batch and continuous flow column experiments.
| MATERIALS AND METHODS |
|---|
|
|
|---|
Chemical Preparation and Analysis
Ethanol was used to initially dissolve the stock 14C labeled 17ß-estradiol and the estrone in a 0.001M CaCl2 solution. The percentages of the ethanol in each batch solutions were 0.163 and 0.125% for 17ß-estradiol and estrone, respectively. The percentage of ethanol in the initial concentration of the column experiment was 0.17%. All these ethanol concentrations were <0.5%, which has been shown not to affect the sorption of an organic pollutant to soil (Wauchope and Koskinen, 1983). The initial radioactivity of the 14C 17ß-estradiol (specific activity = 4.21 x 1014 dpm kg1) in the batch experiments ranged from 14230 dpm to 761869 dpm, and the minimal radioactivity detected was 560 dpm, which was equivalent to 1.7 x104 mg L1. The initial radioactivity for the 14C estrone (specific activity = 4.18 x 1014 dpm kg1) in batch experiments ranged between 5536 dpm to 509407 dpm, and the minimal radioactivity detected was 213 dpm, which was equivalent to 6.4 x105 mg L1. For the column experiment, 124.3 µg 14C 17ß-estradiol was mixed with 8518 µg of 12C 17ß-estradiol in 1.73 L to create the application concentration of 5.0 mg L1. The total 14C labeled 17ß-estradiol (specific activity = 5.96 x 1012 dpm kg1) applied in the column experiment was 5.2 x107 dpm and the minimal dpm detected in the effluent was 42 dpm, which was equivalent to 4.1 x 106 mg L1.
Several analytical procedures were used to determine the concentrations of 17ß-estradiol and its metabolites in the experiments. Liquid scintillation counting was used to analyze for total 14C, and thin-layer chromatography (TLC) was used to analyze for metabolites of 14C 17ß-estradiol. Liquid chromatography/mass spectrometer (LCMS) was also used to analyze selected samples from the column transport experiments. Liquid scintillation counting was done using a 1900 CA Scintillation Counter (Packard, Downers Grove, IL), and TLC analysis was done using a System 2000 Imaging Scanner (Bioscan, Washington, DC). Thin-layer chromatography was conducted using silica gel plates (250 mm; Whatman Lab. Div., Clinton, NJ) and a 25:25:50 tetrahydrofuran/ethyl acetate/hexane mobile phase. A combustion analysis assay (Packard Model 307 Oxidizer; Downers Grove, IL) was also used to determine total 14C sorbed to the soil.
The liquid chromatograph system of the LCMS was an Alliance 2695 Separation Model (Waters, Beverly, MA) equipped with a Symmetry C18 column (3.5 µm, 2.1 by 100 mm), a C18 guard column (2.1 by 10 mm), and a quadrupole-time of flight mass spectrometer (Waters Q-TOF Ultima API-US; Waters, Beverly, MA). A linear binary gradient pump was used, which consisted of 95/5 aqueous 7.4 mM NH4OH/acetonitrile (A) and 100% acetonitrile containing 7.4 mM NH4OH (B). The linear gradient that was used began with 40% B at time 0 min and increased to 100% B at 10 min. The flow rate of the mobile phase was 0.2 mL min1. The mass spectrometer analysis was performed in negative ion mode (ES) with capillary and cone voltages of 2.33 and 55, respectively; source and desolvation temperatures of 120 and 400°C, respectively; and desolvation gas flows of 0 and 500 L h1, respectively. The LCMS sample injection volumes were always 10 µL, and 25 pg mass on column could be reliably detected using selected ion monitoring.
Batch Experiments
In 10-mL vials, 1.6 g of soil and 8 mL of 0.0l M CaCl2 were added. The 14C solution was then added to the vials to create solution concentrations of 0.0015, 0.015, 0.0825, and 0.150 mg L1 for 17ß-estradiol and 0.0014, 0.014, 0.076, and 0.138 mg L1 for estrone. These concentrations were chosen because they span the range of concentrations reported for manures that are applied to fields (Shore et al., 1993, 1995; Finlay-Moore et al., 2000). Each batch experiment was replicated three times. The soilwater slurries were agitated by rotation of the vials top to bottom (360°/5 s). After 0.5, 1, 5, 24, and 48 h, the bottles were centrifuged at 1000 x g (1700 rpm), 100 µL aliquots were removed, and the solution was analyzed using the liquid scintillation and TLC methods described earlier.
Batch Sorption Model
The aqueous concentrations (C; mg L1) of steroidal estrogens will decrease at the same time the sorbed phase concentrations (S; mg kg1) increase. The mass balance of the solute partitioning through time can be expressed with the following ordinary differential equation when sorbed phase degradation (µs; h1) is considered as follows:
![]() | [1] |
The following first-order expression was used as the driving force of sorption through time, as follows:
![]() | [2] |
is the sorption rate coefficient (h1) and Kd (L mg1) is the linear distribution coefficient between the sorbed and aqueous phases. At equilibrium S = Kd x C.
Equation [1] was solved in a spreadsheet using an Euler numeric method with a time step of 0.001 h. This solution was done by coupling Eq. [2] with the following ordinary differential equation as follows:
![]() | [3] |
(ti, b), which corresponds to a trial vector of parameter values b, where b is the vector of optimized parameters
, Kd, and µs. An optimum combination of parameters bo is then sought to minimize the following objective function:
![]() | [4] |
For all our calculations, S was determined by mass-balance difference (i.e., whatever mass of 14C not present in solution was considered to be sorbed). No metabolites were detected in the aqueous phases so it was assumed that transformations took place in the sorbed phase. It was also possible that transformations took place in the aqueous phase and then quickly reabsorbed to the solid, but this was assumed not to happen. The µs value that we obtained from the column experiment was considered in the numerical solution of Eq. [1] to determine the affect of sorbed phase transformation on the batch Kd estimates.
Column Transport Experiments
A glass column with diameter of 0.03 m was packed with 0.047 kg of dry soil to a length of
0.074 m. The column was saturated from the bottom up over 24 h using a solution of 0.01 M CaCl2. After the column was saturated, steady state flow was established through the column using the same 0.01 M CaCl2 solution. The steady state pore-water velocity was 0.145 m h1. Once steady state velocity was achieved a CaCl2 breakthrough curve was run to characterize the transport of a nonreactive solute (i.e., Cl) through the column. This was done by applying a 5.16 pore volume pulse of 0.05 M CaCl2 solution to the column, followed by the application of the 0.01 M CaCl2 solution. The column effluent was collected in approximately 0.13 pore volume increments and analyzed using an ion-specific electrode. The 0.01 M CaCl2 solution was applied for several pore volumes, after which a 1.721-L (44 pore volume) pulse of 5.00 mg L1 17ß-estradiol in 0.01 M CaCl2 was applied to the column, followed by 0.01 M CaCl2 without 17ß-estradiol for approximately 66 pore volumes. The effluent was collected in 0.1 pore volume increments and analyzed for total 14C and metabolites using scintillation counting and TLC, respectively, with LCMS analysis on selected samples. The total duration for the 17ß-estradiol breakthrough curve experiment was approximately 42 h and the total mass of 14C 17ß-estradiol applied to the column during this time was 8.605 mg.
When the column experiment was complete, the soil was extruded from the glass column in approximately 1-cm increments. This was done to identify the redistribution of the 14C with soil depth. The soil was then analyzed for total 14C using combustion analysis. Sequential solution extraction was done by eluting with toluene, ethyl acetate, and finally methanol in the cell of an accelerated solvent extractor (ASE, model 200; Dionex, Sunnyvale, CA). Liquid scintillation was done on all ASE extractions to quantify total 14C. Also, TLC was used to detect any metabolites in these extractions.
Column Transport Model
The CaCl2 and 17ß-estradiol miscible-displacement experiments were inversely modeled using the program HYDRUS-1D version 2.0 (
im
nek et al., 1998). This inverse model routine uses a least-squares method that minimizes an objective function, which provides a best-fit model solution to the measured transport data. The best-fit model solution to the transport data is obtained by finding the optimum combination of reaction and transport parameters. The code of HYDRUS-1D was modified to inversely model two solutes involved in a transformation chain reaction.
Two model variations, one with instantaneous sorption and the other with time dependent sorption, were used to describe the transport data. In both model variations it was assumed that the solute was transported in the aqueous phase by convection and dispersion, and that there was a first-order transformation reaction of 17ß-estradiol into estrone. The following differential equations represent the convectivedispersive transport of a solute undergoing transformation (van Genuchten, 1985), and instantaneous or time-dependent sorption (Selim et al., 1977; van Genuchten and Wagenet, 1989) as follows:
![]() | [5] |
![]() | [6] |
b is soil bulk density (kg m3),
is the volumetric water content (m3 m3),
(m) is the dispersivity, v is steady state pore velocity (m h1), x is depth (m), and µs' is a first-order transformation rate constant in the solid phase (h1) that provides connection between parent and daughter compounds. In Eq. [5] and [6], when sorption is considered to be only instantaneous then
![]() | [7] |
![]() | [8] |
![]() | [9] |
![]() | [10] |
is a first-order sorption rate coefficient (h1). To model the CaCl2 breakthrough, Eq. [5] was used with no transformations or sorption (i.e., µ's1 = S1 = 0), and
was estimated. | RESULTS AND DISCUSSION |
|---|
|
|
|---|
Sorption Kinetics and Degradation
The slopes of the sorption isotherms of 17ß-estradiol and estrone (Fig. 1a and 1b)
increased through time, and aqueous concentration decreased through time (Fig. 2a and 2b)
. These results indicated that there was a kinetic process occurring, which may be explained by sorption kinetics, degradation, or a combination of these processes. In this section we look at the effect of sorbed phase degradation and sorption kinetics on the interpretation of the 17ß-estradiol batch experiments. We assumed that if degradation occurred, then it was in the sorbed phase, because no metabolites were detected in the aqueous phase. Equation [1] was fit to the time series of C values (e.g., Fig. 2a) using a fixed µ's value obtained from the column experiment (µs = 0.09 h1, presented later) and optimizing
and Kd. The optimized
and Kd values were 0.44 h1 and 41.00 L kg1, respectively, and the model fit was excellent for the measured points
5 h (r2 = 0.99). However, at times
24 h, the µs of 0.09 h1 provided an over-prediction of 17ß-estradiol dissipation. This model solution predicted a continual decrease in concentrations instead of approaching a more steady value, as our data indicated (Fig. 2a and 2b). This result suggests that within the first 24 to 48 h sorption kinetics was more significant than degradation, because the aqueous concentrations converged to an apparent constant rather than continually decreasing as a result of degradation (Fig. 2).
|
|
524 h) for hormone sorption has been observed in other studies (Lai et al., 2000; Holthaus et al., 2002; Yu et al., 2004). Our 24 to 48 h log Koc (log Koc = log10[Kd/(OC/100)] values for 17ß-estradiol (
3.2) and estrone (
3.3) were comparable to values reported by other studies for soil. Yu et al. (2004) reports log Koc values for 17ß-estradiol that range from 3.14 to 5.38 and estrone values that range from 3.3 to 5.25. Lee et al. (2003) also report values for 17ß-estradiol that range from 3.21 to 3.46 and estrone values that range from 3.19 to 3.22. Lee et al. (2003) indicate that the primary sorption domain for the estrogen hormones is organic C, and that partitioning is consistent with hydrophobic partitioning process; that is, there is a direct linear correlation between the log10 octanolwater portioning coefficient (log Kow) and log Koc. Our 24-h log Koc values (Table 1) were used to calculate the log Kow values using the Means et al. (1980) linear relation, where log Koc = log Kow 0.317. The calculated log Kow values for 17ß-estradiol and estrone were 3.25 and 3.28, respectively, and fell within the range of values reported in the literature, which was 3.10 (Hansch et al., 1995) to 4.01 (Suzuki et al., 2001) for 17ß-estradiol, and 2.45 (Suzuki et al., 2001) to 3.43 (cited by Lai et al., 2000) for estrone. This result suggests that the log Koc information is useful in predicting partitioning of these estrogens.
|
and Kd values were used to model the data for each initial concentration of both 17ß-estradiol (
= 0.178 h1, Kd = 86.00 L kg1) and estrone (
= 0.210 h1, Kd = 94.00 L kg1). This model provided excellent descriptions of the sorption data for 17ß-estradiol (r2 ranged from 0.94 to 0.98 with mean of 0.98) and estrone (r2 ranged from 0.94 to 1.00 with mean 0.98). This sorption data obeyed Fick's law, where sorption was found to be linear and proportional to the square root of time, and
was the same for each C0 (Rogers, 1965). Pignatello and Xing (1996) indicate that this type of Fickian behavior is consistent with sorption of dilute contaminants (penetrant concentrations in this study
1 x 107 to 1 x 105 kg kg1) into soft organic C or the amorphous organic matter domain. Others (e.g., Brusseau et al., 1991; Luthy et al., 1997; Xing et al., 1996) have also observed this type of rate-limited diffusion process. The 17ß-estradiol batch data from the Casey et al. (2003) study were revisited to see whether the data were consistent with our current study. The sorption model (Eq. [1]) described the Casey et al. (2003) batch data well for the various soils (see r2 values presented in Table 2). The resulting log Koc values (Table 2) were consistent with the values of the current study (Table 1). These log Koc values increased with time, which was also similar to the current study. There was a negative correlation between log Koc values and OC (correlation coefficient = 0.872), which indicated that other nonhydrophobic processes contributed to sorption. The predominant sorption process remains hydrophobic as Lee et al. (2003) demonstrates; however, the contribution of other nonhydrophobic processes increases as OC decreases, and the apparent Koc values increase. One explanation for nonhydrophobic sorption is provided by Yu et al. (2004), who suggests that the phenolic group of 17ß-estradiol and estrone can interact with humic acids or mineral surfaces via hydrogen and covalent bonding. They propose that the polar groups at the C-17 position of both molecules can react with humic acids and mineral surfaces causing sorption to follow some specific interactions in addition to hydrophobic interactions.
|
|
|
value of 0.024 m. The model fit to the Cl breakthrough curve was good (r2 = 0.98) and indicated that transport was a physical equilibrium process. The breakthrough curves of 17ß-estradiol, estrone, and total 14C were all asymmetric (Fig. 4)
. The asymmetric breakthrough curves indicated chemical nonequilibrium transport of the estrogens and not physical nonequilibrium, because the CaCl2 was transported as a physical equilibrium process. Instantaneous and two-site sorption scenarios were considered in modeling the estrogen breakthrough curves. For two-site sorption, sorption takes place on both instantaneous and kinetic sites, and there is a fixed ratio (f) between these two sorption sites (van Genuchten and Wagenet, 1989). The batch sorption parameters (Tables 1) and the
value from the CaCl2 column experiment were fixed in our initial model runs, whereas µs' and f values were estimated. Then, various model parameters were optimized to obtain a better model description of the data. Also, the 17ß-estradiol and estrone breakthrough curves were optimized simultaneously, which improves the uniqueness of parameter estimates (Casey and
im
nek, 2001).
|
Das et al. (2004) used a two-site sorption model (van Genuchten and Wagenet, 1989) to describe estrogen breakthrough curves from a 1.0-cm long soil column. The two-site sorption concept was also appropriate for describing our breakthrough curves, because there appeared to be a rate-limiting sorption process, which caused the breakthrough curve tail and was observed in our batch experiments. In the first two-site sorption model simulation (Table 3, two-site/1), Kd and
were fixed to values obtained from the batch study (Kd1 = 86.00 L kg1, Kd = 94.00 L kg1,
1 = 0.18 h1,
2 = 0.21 h1) and µ's1, µ's2, and f were optimized. The SSQ value for this simulation was reasonable. However, the peak concentrations of 17ß-estradiol were underestimated, and the tail of the estrone was over-predicted (fit not shown). Still, the two-site sorption model option was able to capture the shape of the breakthrough curve better than the instantaneous sorption option using the batch determined parameters.
The two-site sorption model was fit to the breakthrough data again using fixed values of
,
1, and
2, while optimizing for µ's1, µ's2, Kd1, Kd2, and f (Table 3; two-site/2). The Kd values were estimated because it was not clear from the batch experiments how degradation/transformation affected this parameter. The number of parameters that were estimated was five, which appears to be large. However, there were two breakthrough curves or 2.5 parameters estimated per curve, which is not unreasonable. The model fit was excellent (Fig. 4b; SSQ = 0.028) and the confidence intervals of the parameter estimates were narrow (Table 3), which indicates a more unique solution. The Kd estimates for 17ß-estradiol and estrone fell within the range of values calculated from the batch studies. Also, the 17ß-estradiol µ's estimate was similar to values reported by Colucci et al. (2001), but the estrone µ's value was higher than the 17ß-estradiol value. Das et al. (2004) found that estrone degraded faster than 17ß-estradiol for their flow-interruption soil column experiment. The
values from the batch experiments provided a good prediction of the breakthrough curve tail. Also, the f value indicated that about one-sixth of the sorption sites were instantaneous or readily available to sorption.
To further evaluate the confidence in these column parameter estimates, the 17ß-estradiol Kd1,
1, and µ's1 values (Table 3, two-site/2) were used to solve the kinetic sorption model, Eq. [2]. This solution was then compared with the 17ß-estradiol batch aqueous concentrations through time. This model provided a good description of the batch data through 5 h (r2 = 0.95, SSQ = 0.001), but at times
24 h this solution over-predicted the dissipation of 17ß-estradiol. This result may suggest that degradation slows as aqueous concentrations decrease, and may not, as Das et al. (2004) suggests, follow a first-order process. This may also explain why the aqueous 17ß-estradiol concentrations in the batch experiments did not go to zero but approached an apparent constant. Lastly, the two-site sorption option and parameter estimates (Table 3, two-site/2) were used to predict profile distribution of 17ß-estradiol and estrone, and compared well to the measured distribution of these hormones (Fig. 3). This further confirmed the confidence in this model and these parameter estimates.
| CONCLUSIONS |
|---|
|
|
|---|
| ACKNOWLEDGMENTS |
|---|
| REFERENCES |
|---|
|
|
|---|
im
nek, and G.L. Larsen. 2004. Fate and transport of testosterone in agricultural soils. Environ. Sci. Technol. 38:790798.[Medline]
im
nek. 2003. Fate and transport of 17ß-estradiol in soilwater systems. Environ. Sci. Technol. 37:24002409.[Medline]
im
nek. 2001. Inverse analyses of the transport of chlorinated hydrocarbons subject to sequential transformation reactions. J. Environ. Qual. 30:13541360.
im
nek, J., M.
ejna, and M.Th. van Genuchten. 1998. The HYDRUS-1D software package for simulating the one-dimensional movement of water, heat, and multiple solutes in variably-saturated media. Version 2.0. IGWMC-TPS-70. Int. Ground Water Modeling Center, Colorado School of Mines, Golden, CO.This article has been cited by other articles:
![]() |
M. Unold, J. Simunek, R. Kasteel, J. Groeneweg, and H. Vereecken Transport of Manure-Based Applied Sulfadiazine and Its Main Transformation Products in Soil Columns Vadose Zone J., August 11, 2009; 8(3): 677 - 689. [Abstract] [Full Text] [PDF] |
||||
![]() |
M. Laegdsmand, H. Andersen, O. H. Jacobsen, and B. Halling-Sorensen Transport and Fate of Estrogenic Hormones in Slurry-treated Soil Monoliths J. Environ. Qual., March 25, 2009; 38(3): 955 - 964. [Abstract] [Full Text] [PDF] |
||||
![]() |
J. D. Wilcox, J. M. Bahr, C. J. Hedman, J. D. C. Hemming, M. A. E. Barman, and K. R. Bradbury Removal of Organic Wastewater Contaminants in Septic Systems Using Advanced Treatment Technologies J. Environ. Qual., January 13, 2009; 38(1): 149 - 156. [Abstract] [Full Text] [PDF] |
||||
![]() |
S. A. Bradford, E. Segal, W. Zheng, Q. Wang, and S. R. Hutchins Reuse of Concentrated Animal Feeding Operation Wastewater on Agricultural Lands J. Environ. Qual., September 2, 2008; 37(5_Supplement): S-97 - S-115. [Abstract] [Full Text] [PDF] |
||||
![]() |
H. A. Sangsupan, D. E. Radcliffe, P. G. Hartel, M. B. Jenkins, W. K. Vencill, and M. L. Cabrera Sorption and Transport of 17{beta}-Estradiol and Testosterone in Undisturbed Soil Columns J. Environ. Qual., October 27, 2006; 35(6): 2261 - 2272. [Abstract] [Full Text] [PDF] |
||||
| ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
| HOME | HELP | FEEDBACK | SUBSCRIPTIONS | ARCHIVE | SEARCH | TABLE OF CONTENTS |
| The SCI Journals | Agronomy Journal | Crop Science | |||
| Journal of Natural Resources and Life Sciences Education |
Vadose Zone Journal | ||||
| Soil Science Society of America Journal | Journal of Plant Registrations | The Plant Genome | |||