| Literature DB >> 35205055 |
Drew J Hansen1, Alex J Horne2.
Abstract
The retention of heavy metals in water treatment wetlands is well documented, but little understood. Fluxes to and from sediments for moderate concentrations of dissolved metals are particularly unknown. Treatment wetlands are dried out seasonally or occasionally for maintenance. The extent to which heavy metals may be released by drying/re-flooding is of particular concern because of the potential for toxic levels of metals to be mobilized. A 36 ha treatment wetland receiving treated oil refinery effluent in California was dried for 6 months, then re-flooded to an average depth of >10 cm. The concentrations of 11 metals, As and Se in inflow, outflow, and porewaters were measured weekly for 4 months. Mass flux rates showed that the wetland acted as a sink for As and Se, six metals (Co, Cr, Mg, Mn, Ni, and Sr) and S were overall sources and five showed zero net flux (Ba, Cu, Fe, Mo, and Zn). Porewater results indicate that oxidation of the sediments caused the source metals to be released. Removal for As > Cu, Fe, Mo, Zn > Co, Mn, Ni was consistent with the thermodynamically-predicted 'sulfide ladder', suggesting that available sulfide was insufficient to re-sequester the entire pool of mobile chalcophile elements. Our results suggest that less-soluble sulfide metals may be immobilized prior to more-soluble metals following drying/re-flooding in coastal systems with multiple metal contaminants. Ponding for up to several weeks, depending on the metals of concern, will facilitate metal re-immobilization within sediments before waters are released and minimize impacts downstream. Research on how to speed-up the conversion of soluble metals to their insoluble sulfides or other immobilized forms is urgently needed.Entities:
Keywords: arsenic; re-flooding; sediment oxidation; selenium; trace metals; treatment wetland
Year: 2022 PMID: 35205055 PMCID: PMC8869573 DOI: 10.3390/biology11020188
Source DB: PubMed Journal: Biology (Basel) ISSN: 2079-7737
Figure 1(a) The Chevron wetland in relation to San Francisco Bay; (b) schematic of the wetland showing generalized water flow and location of the primary study site in Pass 1.
The 16 week mean values (±standard deviation) for pH, electrical conductivity (EC), and redox potential (Eh) measured in wetland inlet, outlet (n = 16), and porewaters (n = 60–80).
| pH | EC (µS cm−1) | Eh (mV) | |
|---|---|---|---|
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| 7.34 ± 0.22 | 3600 ± 700 | 281 ± 251 |
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| 7.31 ± 0.19 | 4100 ± 400 | 288 ± 241 |
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| 7.18 ± 0.20 | 6200 ± 2500 | 222 ± 294 |
Figure 2Zero-flux elements: Ba, Cu, Fe, Mo, and Zn. Periodic (4 week) mean values for: (A) Inlet, Outlet, and Porewater concentrations (µg or mg * L−1 ± standard deviation; n = 4 for inlet and outlet; n = 15–30 for porewater); (B) rates of mass removal (g or kg * day−1 ± standard error); and (C) percent of mass removed from inflow (±standard error) during the 16 week study period.
Figure 3Source elements: S and Sr. Periodic (4-week) mean values for: (A) Inlet, Outlet, and Porewater concentrations (µg or mg * L−1 ± standard deviation; n = 4 for Inlet and Outlet; n = 15–30 for Porewater); (B) Rates of mass removal (g or kg * day−1 ± standard error); and (C) Percent of mass removed from inflow (±standard error) during the 16-week study period.
Pooled (16 week) mean values for total metal, As, Se and S concentrations in inlet, outlet and porewaters (µg or mg */L ± standard deviation), removal rate (g or kg **/day ± standard error) and percent removed from inlow (±standard error) for Sink, Zero-flux and Source elements measured during the study period. Value superscripts (a–c) indicate statistically significant differences (ANOVA, p < 0.05, Tukey–Kramer). (n = 16 for inlet and outlet values; n = 60–80 for porewater values). Selected solubility product constants for sulfide minerals corresponding to the measured metal(loid)s.
| Elements | Inlet Concentration | Outlet Concentration | Porewater Concentration | Rate of Mass Removal | Percent Removed from Inflow | Log K′sp of Sulfide Mineral § |
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§ Selected solubility products for orpiment (As2S3), covellite (CuS), mackinawite (FeS), pyrite (FeS2), molybdenite (MoS2), sphalerite (ZnS), cobalt sulfide (CoS), albandite (MnS) and millerite (NiS), respectively. Data are from the Minteq.v3 database [41]. Solubility products were adjusted for ionic strength (I = 0.1) using porewater conductivity data [42] and the Davies equation [43]. n.a. = not applicable, n.d. = no data. ¶ The solubility of orpiment (As2S3) would be expected to increase under the pH conditions of this study [44]. # Metal-selenides should form before corresponding metal sulfides because they are thermodynamically less soluble (e.g., Log Ksp = −33.1 (CuSe); −11 (FeSe); −14.4 (ZnSe); −16.2 (CoSe); −3.5 (MnSe); −17.7; (NiSe)) [41]. † Mackinawite forms before pyrite under the study conditions due to faster reaction kinetics [13]. ‡ The formation of MoS2 under wetland conditions is thought to be kinetically limited (requiring temperatures > 200 °C) and is likely mediated by sulfate-reducing bacteria [45].
Figure 4Sink elements: As and Se. Periodic (4 week) mean values for: (A) Inlet, Outlet, and Porewater concentrations (µg L−1 ± standard deviation; n = 4 for inlet and outlet; n = 15–30 for porewater); (B) rates of mass removal (g day−1 ± standard error); and (C) percent of mass removed from inflow (±standard error) during the 16 week study period.