Methiocarb Degradation by Electro-Fenton - Ecotoxicological Evaluation
At a Glance
Section titled âAt a Glanceâ| Metadata | Details |
|---|---|
| Publication Date | 2020-12-12 |
| Journal | Molecules |
| Authors | FalĂ©stine Souiad, Ana Sofia Rodrigues, Ana Lopes, Lurdes CirĂaco, Maria JosĂ© Pacheco |
| Institutions | Université Constantine 2, University of Beira Interior |
| Citations | 11 |
| Analysis | Full AI Review Included |
Executive Summary
Section titled âExecutive SummaryâThis study investigates the efficacy of the Electro-Fenton (EF) process, utilizing a Boron-Doped Diamond (BDD) anode and a carbon felt cathode, for the degradation and detoxification of the highly hazardous pesticide Methiocarb (MC).
- High Degradation Efficiency: Total MC removal (>99%) was achieved rapidly across all tested conditions, requiring only 40 minutes of treatment or an applied electric charge of 120 C.
- Significant Detoxification: The EF process resulted in a drastic reduction in acute toxicity towards the model organism Daphnia magna, achieving an average reduction factor of 450x (from approximately 900 Toxic Units (TU) to ~2 TU).
- Optimal Mineralization Conditions: The highest Total Organic Carbon (TOC) removal (>90%) was obtained at the lowest tested parameters: 10 mg L-1 iron concentration and 12.5 A m-2 applied current density.
- Mechanism Insight: Higher TOC removal at low current densities suggests that organic oxidation via hydroxyl radicals adsorbed on the BDD anode surface (BDD(OH)) is highly effective for mineralization.
- Catalyst Flexibility: No significant differences in MC removal rates were observed between the two iron sources tested (ferric sulfate vs. ferric chloride).
- Process Comparison: The EF process is confirmed as a feasible alternative to Anodic Oxidation (AO) for remediation, achieving similar final detoxification levels despite the initial increased toxicity caused by the added iron salts.
Technical Specifications
Section titled âTechnical Specificationsâ| Parameter | Value | Unit | Context |
|---|---|---|---|
| Anode Material | Boron-Doped Diamond (BDD) | N/A | High O2-overpotential |
| Cathode Material | Carbon Felt | N/A | H2O2 electrogeneration |
| Anode Immersed Area | 20 | cm2 | Geometric area |
| Cathode Immersed Area | 130 | cm2 | Geometric area |
| Initial Methiocarb Concentration | 20.0 ± 0.6 | mg L-1 | Model aqueous solution |
| Initial pH | 2.81 to 3.34 | N/A | Optimum range for EF |
| Applied Current Density (j) | 12.5, 25, 50 | A m-2 | Experimental variables |
| Iron Concentration ([Fe3+]) | 10, 30 | mg L-1 | Experimental variables |
| Total MC Removal Charge | 120 | C | Required for >99% removal |
| Maximum TOC Removal | >90 | % | Achieved at 12.5 A m-2, 10 mg L-1 Fe |
| Initial Acute Toxicity (TU) | 883.1 to 929.4 | TU | Highly Toxic classification |
| Final Acute Toxicity (TU) | 1.96 to 2.02 | TU | Toxic/Non-Toxic classification (after 720 C) |
| Toxicity Reduction Factor | 450 | x | Average reduction achieved |
Key Methodologies
Section titled âKey MethodologiesâThe Electro-Fenton (EF) experiments were conducted in a batch reactor setup using controlled electrochemical and chemical parameters:
- Solution Preparation: Methiocarb (MC) solutions (20 mg L-1) were prepared using ultrapure water. Iron catalyst was introduced as either Iron(III) sulfate pentahydrate (Fe2(SO4)3·5H2O) or ferric chloride hexahydrate (FeCl3·6H2O) to achieve concentrations of 10 or 30 mg L-1 Fe.
- Reactor Configuration: A 200 mL undivided cylindrical glass cell was used, maintained under continuous magnetic stirring to enhance mass transport.
- Electrode Placement: A Boron-Doped Diamond (BDD) electrode (20 cm2 immersed area) served as the anode, centered within the cell. A carbon felt piece (130 cm2 immersed area) served as the cathode, covering the inner wall.
- Oxygen Supply: Compressed air was continuously bubbled into the solution at 1 L min-1, starting 10 minutes before the assay, to ensure continuous in situ electrogeneration of H2O2 at the cathode.
- Electrochemical Operation: A DC power supply was used to maintain constant anodic current densities (j) of 12.5, 25, or 50 A m-2. Experiments were run until an applied electric charge of 720 C was reached for final analysis.
- Analytical Monitoring: MC decay was tracked using High-Performance Liquid Chromatography (HPLC). Mineralization was assessed by measuring Total Organic Carbon (TOC). Dissolved Fe2+ and H2O2 concentrations were determined spectrophotometrically.
- Ecotoxicity Assessment: Acute toxicity was evaluated using the Daphtoxkit F microbiotest, measuring the 48 h EC50 (concentration causing 50% immobilization) of Daphnia magna neonates.
Commercial Applications
Section titled âCommercial ApplicationsâThe BDD-based Electro-Fenton technology demonstrated in this research is highly relevant for advanced environmental engineering applications, particularly in the treatment of persistent organic pollutants (POPs).
- Pesticide and Herbicide Remediation: Direct application in treating agricultural runoff and industrial wastewater streams contaminated with carbamate pesticides (like Methiocarb) and other recalcitrant organic compounds.
- Advanced Oxidation Processes (AOPs): Integration of the EF system as a high-efficiency tertiary treatment stage in municipal or industrial wastewater treatment plants to achieve final detoxification and high mineralization indexes.
- BDD Electrode Technology: Increased demand for high-performance BDD anodes in electrochemical reactors, valued for their stability, high oxygen overpotential, and ability to generate powerful hydroxyl radicals for bulk and surface oxidation.
- Water Reuse and Recycling: Enabling the safe reuse of contaminated water sources by effectively reducing acute toxicity to aquatic life, a critical step for environmental discharge compliance.
- In Situ Reagent Generation: Utilization of the EF process eliminates the logistical and safety challenges associated with storing and handling bulk chemical oxidants (H2O2), promoting safer and more sustainable water treatment operations.
View Original Abstract
This paper studies the degradation of methiocarb, a highly hazardous pesticide found in waters and wastewaters, through an electro-Fenton process, using a boron-doped diamond anode and a carbon felt cathode; and evaluates its potential to reduce toxicity towards the model organism Daphnia magna. The influence of applied current density and type and concentration of added iron source, Fe2(SO4)3·5H2O or FeCl3·6H2O, is assessed in the degradation experiments of methiocarb aqueous solutions. The experimental results show that electro-Fenton can be successfully used to degrade methiocarb and to reduce its high toxicity towards D. magna. Total methiocarb removal is achieved at the applied electric charge of 90 C, and a 450Ă reduction in the acute toxicity towards D. magna, on average, from approximately 900 toxic units to 2 toxic units, is observed at the end of the experiments. No significant differences are found between the two iron sources studied. At the lowest applied anodic current density, 12.5 A mâ2, an increase in iron concentration led to lower methiocarb removal rates, but the opposite is found at the highest applied current densities. The highest organic carbon removal is obtained at the lowest applied current density and added iron concentration.
Tech Support
Section titled âTech SupportâOriginal Source
Section titled âOriginal SourceâReferences
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