Understanding the Dissolution and Passivation of an Aluminum Electrode during Electrocoagulation of Groundwater Using Neutron and X-ray Reflectometry

An aluminum (Al)-based electrocoagulation (EC) system can effectively remove dissolved silica and hardness in groundwater. The effectiveness of Al-EC in terms of pollutant removal, Faradaic efficiency, and energy consumption depends on the interfacial electrolysis or passivation of the electrode in water. Thus, understanding the electrolysis reaction at the liquid/electrode interface during operation is important for sustainable EC deployment. A continuous flow-through Al-EC system was tested with various groundwater simulants, i.e., chloride (Cl<sup>-</sup>)-based, sulfate (SO<sub>4</sub><sup>2-</sup>)-based, and mixed solutions. High pollutant removal with low energy consumption was observed in Cl<sup>-</sup>-based groundwater treatment, while low pollutant removal with high energy consumption was observed in SO<sub>4</sub><sup>2-</sup>-based groundwater. For example, the required energy per unit mass of Al dosing in SO<sub>4</sub><sup>2-</sup>-based groundwater is three times higher than that in Cl<sup>-</sup>-based groundwater at 10 mA/cm<sup>2</sup>. However, increasing the Cl<sup>-</sup> concentration significantly reduces this energy demand. In SO<sub>4</sub><sup>2-</sup>-based groundwater, the silicate removal efficiency drops from 85.1% to 24.0% compared to that for Cl<sup>-</sup>-based groundwater, while Mg<sup>2+</sup> and Ca<sup>2+</sup> removal efficiencies decrease to 0.6% from 15.8% and 5.7% from 44.8%, respectively. To better understand this EC performance, we used in situ neutron reflectometry (NR) to examine the interfacial dynamics of Al dissolution and passivation at a 100 nm scale occurring on the surface of the sacrificial Al electrodes during EC. Ex situ X-ray reflectometry (XRR) was also used to support the in situ NR results. Both NR and XRR results revealed that Al dissolution is influenced by the presence of Cl<sup>-</sup> in the simulants, while a passivating layer forms on the electrode in a SO<sub>4</sub><sup>2-</sup>-based solution. In the Cl<sup>-</sup>-based solution, anodic Al dissolution occurred locally and inhomogeneously across the surface of the Al anode film, resulting in a localized thickness reduction over time. In the SO<sub>4</sub><sup>2-</sup>-based solution, no apparent dissolution of the Al anode was identified. Instead, Al underwent oxidation, forming an amorphous Al<sub>2</sub>O<sub>3</sub> surface layer within the Al electrode film that increased in thickness over time. In the mixed solution, both anodic Al dissolution and surface Al<sub>2</sub>O<sub>3</sub> layer formation occurred, indicating that Al dissolution and surface Al<sub>2</sub>O<sub>3</sub> layer formation are attributable to the Cl<sup>-</sup> and SO<sub>4</sub><sup>2-</sup> ions, respectively.

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Journal
ACS Applied Materials & Interfaces
Published
2025-04-21
DOI
https://doi.org/10.1021/acsami.5c02215
Citations
3
Primary Topic
Advanced oxidation water treatment
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article
Field-Weighted Citation Impact
2.45

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article

Understanding the Dissolution and Passivation of an Aluminum Electrode during Electrocoagulation of Groundwater Using Neutron and X-ray Reflectometry

Dale K. Hensley, Alexander I. Wiechert, Marta C. Hatzell, Jong K. Keum et al.
3 citations
ACS Applied Materials & Interfaces
Advanced oxidation water treatment
2.45
article

Understanding the Dissolution and Passivation of an Aluminum Electrode during Electrocoagulation of Groundwater Using Neutron and X-ray Reflectometry

Dale K. Hensley, Alexander I. Wiechert, Marta C. Hatzell, Jong K. Keum, Costas Tsouris, David Jassby, James F. Browning, Swapnamoy Dutta, Joshua T. Damron, Gyoung Gug Jang, Candice E. Halbert
article en
3 citations

Abstract

An aluminum (Al)-based electrocoagulation (EC) system can effectively remove dissolved silica and hardness in groundwater. The effectiveness of Al-EC in terms of pollutant removal, Faradaic efficiency, and energy consumption depends on the interfacial electrolysis or passivation of the electrode in water. Thus, understanding the electrolysis reaction at the liquid/electrode interface during operation is important for sustainable EC deployment. A continuous flow-through Al-EC system was tested with various groundwater simulants, i.e., chloride (Cl<sup>-</sup>)-based, sulfate (SO<sub>4</sub><sup>2-</sup>)-based, and mixed solutions. High pollutant removal with low energy consumption was observed in Cl<sup>-</sup>-based groundwater treatment, while low pollutant removal with high energy consumption was observed in SO<sub>4</sub><sup>2-</sup>-based groundwater. For example, the required energy per unit mass of Al dosing in SO<sub>4</sub><sup>2-</sup>-based groundwater is three times higher than that in Cl<sup>-</sup>-based groundwater at 10 mA/cm<sup>2</sup>. However, increasing the Cl<sup>-</sup> concentration significantly reduces this energy demand. In SO<sub>4</sub><sup>2-</sup>-based groundwater, the silicate removal efficiency drops from 85.1% to 24.0% compared to that for Cl<sup>-</sup>-based groundwater, while Mg<sup>2+</sup> and Ca<sup>2+</sup> removal efficiencies decrease to 0.6% from 15.8% and 5.7% from 44.8%, respectively. To better understand this EC performance, we used in situ neutron reflectometry (NR) to examine the interfacial dynamics of Al dissolution and passivation at a 100 nm scale occurring on the surface of the sacrificial Al electrodes during EC. Ex situ X-ray reflectometry (XRR) was also used to support the in situ NR results. Both NR and XRR results revealed that Al dissolution is influenced by the presence of Cl<sup>-</sup> in the simulants, while a passivating layer forms on the electrode in a SO<sub>4</sub><sup>2-</sup>-based solution. In the Cl<sup>-</sup>-based solution, anodic Al dissolution occurred locally and inhomogeneously across the surface of the Al anode film, resulting in a localized thickness reduction over time. In the SO<sub>4</sub><sup>2-</sup>-based solution, no apparent dissolution of the Al anode was identified. Instead, Al underwent oxidation, forming an amorphous Al<sub>2</sub>O<sub>3</sub> surface layer within the Al electrode film that increased in thickness over time. In the mixed solution, both anodic Al dissolution and surface Al<sub>2</sub>O<sub>3</sub> layer formation occurred, indicating that Al dissolution and surface Al<sub>2</sub>O<sub>3</sub> layer formation are attributable to the Cl<sup>-</sup> and SO<sub>4</sub><sup>2-</sup> ions, respectively.

ACS Applied Materials & InterfacesVol. 17(17)
Oak Ridge National Laboratory (US), Georgia Institute of Technology (US), California NanoSystems Institute (US), University of California System (US), Manufacturing Laboratories (United States) (US), NOAA Chemical Sciences Laboratory (US), Center for Nanophase Materials Sciences
Office of Energy Efficiency and Renewable Energy
Clean water and sanitation
Openalex Percentile: Top 12%
Advanced oxidation water treatment
2.45
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