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a Center for the Management, Utilization, and Protection of Water Resources, Tennessee Technological Univ., Dixie Ave., Box 5033, Cookeville, TN 38505-0001
b CSC Engineers, 218C E. Tremont Avenue, Charlotte, NC 28203-5364
c Tennessee Technological Univ., Box 14638, Cookeville, TN 38505-0001
* Corresponding author (gkstearman{at}tntech.edu)
Received for publication June 28, 2002.
| ABSTRACT |
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Abbreviations: EIA, enzyme immunoassay analysis GC, gas chromatography HRTs, hydraulic retention times SAS, Statistical Analysis System SF, subsurface flow TN, Tennessee
| INTRODUCTION |
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Constructed wetlands are a treatment method that contain and remove runoff chemicals by various processes including microbial degradation, plant uptake, sorption, chemical reactions, and volatilization. Constructed wetlands, using a subsurface flow (SF) gravel media, have recently been used to clean wastewater, primarily for N and P (Shannon et al., 2000; Tanner et al., 1998).
Although a limited number of studies examining pesticides have been conducted on SF gravel wetlands, there are several studies reporting pesticide removal in relatively large surface flow wetlands. In a 44-ha vegetated surface flow constructed wetland in South Africa, macrophytes and their associated root dwelling microorganisms were responsible for removing 77 and 93% of influent (0.85 µg L-1) azinphos-methyl (O,OdiethylS-[(4-oxo-1,2,3-benzotriazin-3(4H)-yl) methyl]phosphorodithioate) (an orchard pesticide) and removing most of inlet chlorpyriphos (O,O-diethyl O-(3,5,6-trichloro-2-pyridyl) phosphorothioate) and endosulfan (6,7,8,9,10,10-hexachloro-1,5,5a,6,9,9a-hexahydro-6,9-methano-2,4,3-benzodioxathiepin-3-oxide) at inlet concentrations of 0.02 and 0.2 µg L-1, respectively (Schulz and Peall, 2001). Kadlec and Hey (1994) reported removal of 25 to 95% atrazine (6-chloro-N-ethyl-N'-isopropyl-1,3,5-triazine-2,4-diamine) in reconstructed river wetlands in Des Plains, IL. Detenbeck et al. (1996) reported an atrazine half-life of 8 to 14 d in a 230 m long flow-through wetland.
In a study using a gravel recirculating vertical SF system, McKinlay and Kasperek (1999) concluded that microbial degradation was the dominant process for atrazine decomposition rather than plant uptake. This is the only study (McKinlay and Kasperek, 1999) the authors found that examined pesticide removal in an SF constructed wetland. Tanner et al. (1998) examined maturation of an SF constructed wetland and removal of nitrate and phosphate. As SF gravel constructed wetlands matured, chemical removal changed, especially for phosphate, where sorption was the primary means for removal. As wetland sorption sites were saturated, phosphate removal was reduced (Tanner et al., 1998). Shannon et al. (2000) showed removal of N to increase the second year and removal of phosphate to decrease the second year in an SF constructed wetland system. They attributed increased N removal to increased plant density and decreased phosphate removal to partial saturation of sorption sites.
Several studies have reported atrazine (a triazine herbicide similar in structure to simazine) degradation under anaerobic conditions that may be similar to those found in a gravel constructed wetland. Seybold et al. (2001) reported that in anaerobic soils the half-life was 38 d for atrazine and 62 d for metolachlor. In the aqueous phase above the soil, the half-life was 86 d for atrazine and 40 d for metolachlor. Other researchers have reported differing results for atrazine degradation under anaerobic conditions in wetland soil. Chung et al. (1995) showed that 50% of atrazine degraded in 38 wk under anaerobic conditions. Gu et al. (1992) showed no degradation of atrazine under methanogenic conditions. Delaune et al. (1997) reported slower degradation of atrazine under anaerobic vs. aerobic conditions. Goswami and Green (1971) indicated that atrazine degradation would generally be slower under anaerobic compared with aerobic conditions with sediment, while Kearney et al. (1967) showed that atrazine disappeared more rapidly under anaerobic conditions compared with aerobic conditions. Atrazine fate in sterile and unsterile soil was studied by Kruger et al. (1997), who reported faster atrazine degradation in the surface soil than in the subsoil, but this may be due to increased organic matter rather than increased oxidation. Larsen et al. (2001) showed that atrazine in a wetland soil did not degrade anaerobically after addition of various electron acceptors including nitrate, sulfate, and carbon dioxide.
Metolachlor degradation rates have been reported on a limited basis in anaerobic and strongly reducing conditions (Seybold et al., 2001). Metolachlor was degraded at a greater rate under sulfate reducing conditions than without S present, indicating that possibly sulfate-reducing microorganisms degrade metolachlor (Stamper et al., 1997; Stamper and Tuovinen, 1998).
It is important to determine the required residence time of wastewater in constructed wetlands to adequately reduce the chemicals to nontoxic levels. Some of the removal processes may require hours or days to occur. Since several pesticide removal processes including microbial degradation, chemical hydrolysis/dechlorination, sorption, and plant uptake may occur simultaneously, it is difficult to isolate a single factor that controls pollutant removal in a wetland. Factors that may be important and can be controlled by the design and management of the wetlands include the size and volume of the wetland, the mass loading or flow to the wetlands, and the plant density and composition.
This study examines 14 wetland cells as to the effect of flow (pesticide loading), HRT, presence of plants, depth, and surface area of wetlands on pesticide removal. The objectives of this study were to: (i) determine removal of metolachlor and simazine from container nursery runoff in constructed wetland cells, and (ii) determine the effect of bulrush vegetation, flow, depth, and surface area of constructed wetlands on simazine and metolachlor removal during a 2-yr period from 1998 to 1999.
| MATERIALS AND METHODS |
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3.8 cm in diameter with an effective size of 1.91 cm, and the smaller rock was
2.2 cm in diameter with an effective size of 1.11 cm. Cells A, B, C, D, E, F, and G contained 20 cm of the larger gravel overlaid by 10 cm of the smaller gravel. Cells H, I, J, K, L, M, and N contained 30 cm of the larger size gravel overlaid by 15 cm of the smaller gravel (Fig. 2)
. The purpose of the smaller gravel was to provide firmer bedding material for the plants.
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Container Nursery
A pilot container nursery was constructed on a 35 by 20 m site adjacent to the existing SF wetland system described in the previous section (Fig. 1). Two hundred each of 5-L containerized landscape plants (Monkey Grass, Spiraea, and Japanese Holly) spaced approximately 50 cm apart were grown on this container nursery area. Each plant was potted in a pine barkbased media and fertilized with an 18612 (NPK) slow-release fertilizer before the study.
To facilitate site drainage, the nursery was sloped approximately 1 to 3%. The soil surface was covered with a 0.5-mm thick impermeable polyethylene liner covered with an approximately 15-cm layer of 0.65-cm limestone gravel.
The container bed was irrigated by six overhead rotary impact sprinklers. Manually cleaned, inline filters with a mesh size of 500 cm-1 were installed on each overhead riser to prevent sprinkler clogging. A 745.7-W Hydromatic submersible pump located in the wastewater plant's dechlorination tank provided water to irrigate the nursery. Sulfur dioxide was used to dechlorinate the wastewater treatment plant effluent. The water was transported through 5-cm polyvinyl chloride (PVC) piping throughout the nursery site.
Soil berms were placed around the nursery to prevent intrusion of runoff from outside the nursery area and to ensure that all runoff from the nursery site was collected. Perforated piping was distributed along the lowest end of the site and covered with gravel to transport percolated water to a partially buried 1800-L polyethylene tank. This collected water was pumped to an 8.5-m3 holding tank by a float-controlled, 1491.4-W Hydromatic submersible sump pump. A Shur-Dri 1491.4-W timer-controlled pump subsequently transferred water from the holding tank to the wetland system. The nursery runoff water was distributed by PVC pipe either across the width of the cell or by a single orifice inlet. Lines were flushed for 5 to 10 s each day to prevent clogging. The water level in each cell was controlled by the discharge standpipe elevation (Fig. 2).
Herbicide Application
To simulate a typical weed-management procedure, simazine (Princep) and metolachlor (Pennant) were applied to the gravel surface using an air-pressurized backpack sprayer on 9 July 1998 and 19 May 1999. The liquid Princep was formulated by the Novartis Crop Protection Corporation at 89% pure simazine, 1% related triazines, and 10% inert ingredients. The liquid Pennant product was formulated by the Ciba-Geigy Corporation at 85.1% pure metolachlor and 14.9% inert ingredients. The liquid pesticide formulations were measured using a graduated cylinder and thoroughly mixed with water in a 20-L bucket before pouring the pesticide solution in the backpack sprayer. Princep was applied at 4.78 kg ha-1 (220 g) and Pennant was applied at 2.39 kg ha-1 (110 g) in 1998 and at one-half these rates in 1999.
System Operation
The container nursery was irrigated from 0700 to 0900 h each morning. Irrigation was automatically controlled by an Intermatic 24-h dial time switch (Model T104), which activated the submersible pump in the dechlorination tank of the water treatment plant. Once the water reached the container nursery, a Toro Vision II Plus Series Controller (Model V2-PO6) operated the solenoid valves, allowing flow to specific sprinklers. The average irrigation rate was 0.7 cm h-1, producing approximately 6.05 m3 of nursery runoff each day.
Nursery runoff was applied to all 14 wetland cells using peristaltic pumps with microprocessor pump controllers. The pumps were started manually and operated for 2 h at the same time each day (09001100 h) at flow rates of 0.120, 0.06, and 0.03 m3 h-1. Total water entering cells daily was 0.240, 0.120, and 0.06 m3. The pumps were calibrated weekly during pesticide sampling by volumetrically measuring the quantity of influent into a cell in a 1-min period and comparing this measurement to the flow rate setting on the pump controllers. If necessary, the pump controllers were adjusted accordingly. The flow rates, physical dimensions, and theoretical retention time for each SF cell are listed in Table 1 . Evapotranspiration of cells was measured several times over the course of the experiments and did not vary significantly over the 1-d sampling time. Therefore, evapotranspiration of cells was considered constant and not significantly variable over sampling dates.
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Effluent water samples were analyzed by EIA for simazine and metolachlor. Enzyme immunoassay analysis of selected pesticides and herbicides has been shown to be a practical and cost-effective method (Stearman et al., 1997). Goh et al. (1992) and Leavitt et al. (1991) reported that the EIA of atrazine corresponded analogously with gas or liquid chromatography analysis.
Each of the simazine and metolachlor EIA kits consisted of 96 antibody-coated wells in a microtiter plate and solutions or reagents and standards (Strategic Diagnostics, Newark, DE). Eight standards including a blank were prepared in the same matrix as the collected water samples and were analyzed on the microtiter plate in duplicate. Simazine standard solutions were made over a range of 0.20 to 20 µg L-1 and metolachlor standards ranged from 0.25 to 20 µg L-1.
To provide an accuracy check for the EIA procedure, selected cell effluent samples were analyzed for simazine and metolachlor using gas chromatography (GC) (Method 505, Method 507, U.S. Army Corps of Engineers, 1989). A single 1000-mL sample was obtained from a specific cell during each EIA sampling day starting with Cell A. The sample was collected from the cell effluent standpipe using a prerinsed 60-mL plastic syringe with a 1-mm orifice and transferred immediately to a 1000-mL amber-colored glass jar with a Teflon lid and labeled as previously described. Figures 3 and 4 show the best fit line for the comparison between EIA and GC analysis. For both simazine and metolachlor, EIA and GC were highly correlated. In all cases, EIA results were used to compute pesticide input and pesticide remaining in the wetland cells. Once all cells were sampled (i.e., the end of the 14th day of sampling), the rotation repeated back to Cell A and was continued until the study ceased.
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Organic Carbon Measurement
Organic C from each wetland cell was measured gravimetrically by dry combustion (Davies, 1974). Each wetland cell had eight removable black plastic mesh containers that were removed for sampling the gravel media. After sampling, new mesh containers were filled with gravel and immediately installed to replace the sampled mesh containers in the wetland cells. The sediment was removed from the gravel by scraping and washing the gravel. The resulting sediment solution was dried at 105°C, weighed, and then combusted at 400°C for 4 h and weighed to compute (by difference) the mass of CO2 combusted.
Field Measurements
Probe well clusters, located at one-third intervals in each cell, were installed during the initial wetland construction (Fig. 2). The wells were constructed of PVC pipe and allowed internal sampling at various depths in each wetland cell. Rubber inflatable bladders were inserted in each well to prevent atmospheric oxygen from re-aerating the cell and to allow fresh water to be available for each probe measurement. The bladders were kept inflated until immediately before obtaining measurements, when they were deflated and removed from the well clusters. Dissolved oxygen (DO), water temperature, and pH sensor probes were lowered into the PVC wells until partially submerged in the cell bulk liquid. The meters were allowed to stabilize for approximately 30 to 45 s before a reading was recorded. Probes were rinsed with distilled water before each measurement.
The DO and water temperature measurements were obtained using a Yellow Springs Instrument (YSI) (Yellow Springs, OH) Model 59 Dissolved Oxygen Meter with sealed sampling probe. The pH was measured by an Orion pH meter. Meters were calibrated both before and after sampling. The DO meter was calibrated using the Winkler-Azide method (Method 360.2, USEPA, 1983) while the pH meter was calibrated using premade buffer solutions (Method 150.1, USEPA, 1983).
Data Analyses
Total influent and effluent simazine and metolachlor mass for each cell was computed using the following equation:
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tj,i is 1-d time increment. A general linear model (GLM) (Neter et al., 1990) of the means of the dependent variables simazine and metolachlor was conducted to determine which independent variables (i.e., media depth, presence of vegetation, hydraulic loading or flow, and surface area or aspect ratio) significantly affected herbicide total effluent mass. This method was used to take into account the unbalanced design and unequal subclass distributions within the SF system. The p values were considered significant when
< 0.05. | RESULTS |
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The pH in the SF cells ranged from 6.41 to 7.45, which should be favorable for microbial activity. The cells with plants had pH values that were generally 0.3 units lower than cells without plants.
The percentage of the total influent simazine and metolachlor removed by each constructed wetland cell for the 2 yr is shown in Table 2 . Simazine removal was above 90% of that applied only in vegetated cells with HRTs at or above 13.3 d. Metolachlor removal was above 86% in cells with HRTs at or above 5.1 d.
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| DISCUSSION |
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The nonvegetated cells were more erratic (based on difference between years) in the percent herbicide removed while the vegetated cells had a more uniform removal of herbicides. Possibly, the plant roots contribute to a more uniform environment for microbial degradation. In general, as HRT increased the percent herbicide removed increased (Fig. 5 and 6) . At retention times of 5.1 d, all vegetated cells removed at least 76% of the herbicides. At the high flow rates (high mass loadings) and low retention times, about 60% of the simazine and metolachlor was removed except in Cells B and I for metolachlor, which had 17.9 and 38.8% removal of metolachlor, respectively (Table 2).
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Tables 4 and 5 show the statistical results for years 1998 and 1999 for metolachlor and simazine, respectively. Herbicides were removed at greater percentages at low flow rates compared with high flow rates. As flow increased, mass loading increased, retention time decreased, and percent herbicide removed decreased. Conversely, at the lowest flow rates (highest HRTs) a higher percentage of herbicide was removed, and the HRT was increased allowing more time for removal processes including microbial degradation to occur. On average, constructed wetland cells with plants removed 20.6% more simazine than cells without plants. Planted cells removed 19.2% more metolachlor than nonvegetated cells. Cells with 45 cm depth removed more metolachlor than cells with 30 cm depth, but there was no significant difference for simazine removal with depth of cell. Since flow and depth determine hydraulic residence time, metolachlor removal was highly dependent on residence time while simazine was also to a lesser degree dependent on residence time since flow was significant and depth was not significant. Cells with larger surface area (aspect) were not different in the percent of herbicide removed compared with the cells with less surface area.
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The mass of herbicide applied in 1998 was twice that applied in 1999. Therefore, if mass loading determined pesticide removal, then there should have been differences in percent removal from 1998 to 1999 when examining percent removal for an individual cell. The percent removals shown in Table 2 were not usually different from year to year except in a few cells. Also, there was no difference for pesticide removed between years (Tables 4 and 5). Therefore, mass loading did not appear to be as important as HRT in determining pesticide removal. The cells that had the highest flow rates also had the highest mass loadings and removed the most mass of herbicides but the lowest percent of herbicides. Results show that time is more important than mass loading to achieve removals of 79.3% or more, which were achieved at HRTs above 7.9 d for vegetated cells for both herbicides (Table 2). Also when comparing herbicide removal during the 2-yr sampling period, the pesticide mass entering the cells was much greater initially (immediately after application) and then decreased each week. There was little difference in the daily amounts removed by the cells regardless of high or low mass loading (daily pesticide removal is not shown). This also supports the hypothesis that time was more important than mass loading when examining the percent of pesticide removed. In other words a 2-d retention time may not be enough to remove much more than 60% of the herbicides, no matter what the mass loading.
Flow and volume of cell determine HRT. The HRTs of 2 or 3 d were not long enough for some pesticide removal processes to significantly occur, such as microbial degradation (McCormick and Hiltbold, 1966; Erickson and Lee, 1989; Delaune et al., 1997; Stamper and Tuovinen, 1998). Flow was also equal to mass loading for a particular year, but not between years since pesticide application rates were reduced to half of the first year application rates. The pesticide concentration, combined with flow (i.e., mass loading), should indicate what the system can handle. In this study, even at high mass loadings (1998) the pesticide removals were similar to the subsequent year's removal. By comparing pesticide removal in the vegetated Cells A and H (2 and 3 d HRTs, respectively), which had the same flow (mass loading) and only differed in depth, effects of both depth and HRT could be determined. There was no significant difference between percent removal of herbicides for Cells A and H.
Depth was significant for metolachlor, but not for simazine (Tables 4 and 5). Comparing the pesticide removals in Table 3 shows that the extra 15 cm depth did not improve removals except for a few cells; notably Cell B had only 40.8% removal while the deeper Cell I had 51.6% removal for the combined pesticides. Cells B and I were nonvegetated cells with high flows.
Wetland cells with plants have higher pesticide removals for a number of reasons, including plant uptake, oxygenated rhizosphere zones that enhance aerobic degradation, and increased microbial activity from plant root exudate stimulation.
| SUMMARY AND CONCLUSIONS |
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This 2-yr study found that metolachlor and simazine removal in gravel SF wetlands was significantly improved at lower flow rates with vegetated cells, compared with higher flow rates and nonvegetated cells. The vegetated cell (Cell A) with 2.3-d HRTs removed 62.0% of herbicide applied. The nonvegetated paired Cell B at 2.1-d HRTs removed 40.8% of herbicide applied. The vegetated cell (Cell C) with 5.1-d HRTs removed 82.2% of herbicide applied. The nonvegetated paired Cell D at 4.1-d HRTs removed 64.0% of herbicide applied. Subsurface flow vegetated gravel constructed wetlands can be designed to remove more than 60% of pesticides, metolachlor and simazine.
| ACKNOWLEDGMENTS |
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| REFERENCES |
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