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Predicting ion exchange resin performance for contaminant removal from comingled groundwater plumes

At the U.S. Department of Energy’s Hanford Site, ion exchange (IX) resins Purolite A532E (A532E) and DOWEX 21 K (DOWEX) are used in the 200 West Area (200 W) pump-and-treat (P&T) facility to remove technetium-99 (99Tc, as TcO4-) and uranium (U, as anionic uranyl carbonates, UO2(CO3)n2–2n) from c...

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Published in:Journal of environmental chemical engineering 2024-12, Vol.12 (6), p.114820, Article 114820
Main Authors: Saslow, Sarah A., Pearce, Carolyn I., Levitskaia, Tatiana G., Cordova, Elsa A., Hager, Jacqueline, Fang, Yilin, Escobedo, Nancy M., Johnson, Christian D., Boglaienko, Daria, Torgeson, Joshua, Freedman, Vicky L., Mackley, Rob D.
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container_issue 6
container_start_page 114820
container_title Journal of environmental chemical engineering
container_volume 12
creator Saslow, Sarah A.
Pearce, Carolyn I.
Levitskaia, Tatiana G.
Cordova, Elsa A.
Hager, Jacqueline
Fang, Yilin
Escobedo, Nancy M.
Johnson, Christian D.
Boglaienko, Daria
Torgeson, Joshua
Freedman, Vicky L.
Mackley, Rob D.
description At the U.S. Department of Energy’s Hanford Site, ion exchange (IX) resins Purolite A532E (A532E) and DOWEX 21 K (DOWEX) are used in the 200 West Area (200 W) pump-and-treat (P&T) facility to remove technetium-99 (99Tc, as TcO4-) and uranium (U, as anionic uranyl carbonates, UO2(CO3)n2–2n) from contaminated groundwater. Expansion of 200 W P&T operations will require treatment of new groundwater plumes with variable quantities of other anions, like nitrate, sulfate, carbonate, and chloride. Laboratory batch studies have quantified the impact of varying groundwater chemistry on IX resin performance. However, a demonstration that these laboratory-measured parameters can be used to provide operational feedback to the 200 W P&T facility is required. This work couples hydrologic transport and equilibrium IX coefficients to model contaminant breakthrough from laboratory-scale columns and evaluate scalability by modeling historical 200 W P&T facility data. The approach successfully captures breakthrough of competing groundwater anions, e.g., NO3- and SO42-, and co-contaminants with a lower affinity for the resin IX sites than the target anion. For TcO4- and U carbonate anions targeted by A532E and DOWEX, respectively, the model-derived exchange coefficients are magnitudes larger than those predicted by batch tests. This is attributed to the low, groundwater-relevant contaminant concentrations used in batch tests, where testing a range of contaminant concentrations would be required to confirm the model-derived exchange coefficients. The optimized modeling approach will predict the impact of changes in groundwater chemistry on A532E and DOWEX uptake of 99Tc and U, and open opportunities for predicting P&T response to changes in resin configuration(s) and evaluating the impact of potential new IX resins on P&T performance. •99Tc and U removal by A532E and Dowex 21 K resins quantified under flow conditions.•Exchange coefficients optimized to predict contaminant breakthrough from columns.•Models informed by lab-scale data describe contaminant breakthrough at field-scale.
doi_str_mv 10.1016/j.jece.2024.114820
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Expansion of 200 W P&T operations will require treatment of new groundwater plumes with variable quantities of other anions, like nitrate, sulfate, carbonate, and chloride. Laboratory batch studies have quantified the impact of varying groundwater chemistry on IX resin performance. However, a demonstration that these laboratory-measured parameters can be used to provide operational feedback to the 200 W P&T facility is required. This work couples hydrologic transport and equilibrium IX coefficients to model contaminant breakthrough from laboratory-scale columns and evaluate scalability by modeling historical 200 W P&T facility data. The approach successfully captures breakthrough of competing groundwater anions, e.g., NO3- and SO42-, and co-contaminants with a lower affinity for the resin IX sites than the target anion. 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For TcO4- and U carbonate anions targeted by A532E and DOWEX, respectively, the model-derived exchange coefficients are magnitudes larger than those predicted by batch tests. This is attributed to the low, groundwater-relevant contaminant concentrations used in batch tests, where testing a range of contaminant concentrations would be required to confirm the model-derived exchange coefficients. 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Expansion of 200 W P&T operations will require treatment of new groundwater plumes with variable quantities of other anions, like nitrate, sulfate, carbonate, and chloride. Laboratory batch studies have quantified the impact of varying groundwater chemistry on IX resin performance. However, a demonstration that these laboratory-measured parameters can be used to provide operational feedback to the 200 W P&T facility is required. This work couples hydrologic transport and equilibrium IX coefficients to model contaminant breakthrough from laboratory-scale columns and evaluate scalability by modeling historical 200 W P&T facility data. The approach successfully captures breakthrough of competing groundwater anions, e.g., NO3- and SO42-, and co-contaminants with a lower affinity for the resin IX sites than the target anion. For TcO4- and U carbonate anions targeted by A532E and DOWEX, respectively, the model-derived exchange coefficients are magnitudes larger than those predicted by batch tests. This is attributed to the low, groundwater-relevant contaminant concentrations used in batch tests, where testing a range of contaminant concentrations would be required to confirm the model-derived exchange coefficients. 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subjects 1-D flow
Dowex 21K
Hanford
Performance model
Purolite A532E
Technetium
Uranium
title Predicting ion exchange resin performance for contaminant removal from comingled groundwater plumes
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