Insight into electrochemical degradation of Cartap (in Padan 95SP) by boron-doped diamond electrode - kinetic and effect of water matrices
At a Glance
Section titled âAt a Glanceâ| Metadata | Details |
|---|---|
| Publication Date | 2022-01-01 |
| Journal | TURKISH JOURNAL OF CHEMISTRY |
| Authors | HOANG NGUYEN |
| Institutions | University of Da Nang, Da Nang University of Technology |
| Citations | 2 |
| Analysis | Full AI Review Included |
Technical Documentation: Electrochemical Degradation of Cartap using Boron-Doped Diamond (BDD) Electrodes
Section titled âTechnical Documentation: Electrochemical Degradation of Cartap using Boron-Doped Diamond (BDD) ElectrodesâThis document analyzes the research paper âInsight into electrochemical degradation of Cartap⊠by boron-doped diamond electrodeâ (Nguyen, 2022) to highlight the critical role of high-quality MPCVD Boron-Doped Diamond (BDD) in Advanced Oxidation Processes (AOPs) and wastewater treatment.
Executive Summary
Section titled âExecutive Summaryâ- Application Focus: Electrochemical degradation of the pesticide Cartap (Padan 95SP) using a BDD anode in an Advanced Oxidation Process (AOP).
- Core Mechanism: Degradation occurs via both direct oxidation (15% contribution) and indirect oxidation (85% contribution) driven by highly reactive radicals.
- Dominant Oxidants: Hydroxyl radicals (âąOH) were the primary oxidant (61.5% contribution), followed by sulfate radicals (SOââąâ») (12.8% contribution).
- Material Performance: The BDD electrode demonstrated excellent electrochemical capability, characterized by high stability, corrosion resistance, and a charge transfer resistance of 92.6 Ω.
- Kinetic Enhancement: The presence of 15 mM chloride (Clâ») significantly enhanced the degradation rate constant (kCT) by 38% (from 0.039 minâ»Âč to 0.054 minâ»Âč).
- Scalability Potential: The successful use of BDD in this high-efficiency AOP confirms its suitability for industrial-scale water purification systems targeting refractory organic pollutants.
Technical Specifications
Section titled âTechnical SpecificationsâThe following hard data points were extracted from the BDD electrode characterization and kinetic experiments:
| Parameter | Value | Unit | Context |
|---|---|---|---|
| BDD Exposed Surface Area | 3.8 | cm2 | Working electrode dimension |
| Diamond Layer Thickness | 2.5-3 | ”m | CVD film thickness |
| BDD Substrate Material | Si | - | Silicon substrate |
| BDD Grain Size (Medium) | 200 | nm | Determined by SEM |
| Boron Doping Concentration (EDX) | 15.1 | % | High doping level for conductivity |
| Charge Transfer Resistance (RCT) | 92.6 | Ω | Measured via EIS |
| Applied Current Density (j) | 40 | mA cm-2 | Optimal galvanostatic control |
| Baseline Rate Constant (kCT) | 0.039 | min-1 | At 40 mA cm-2, 0 mM additives |
| Enhanced Rate Constant (kCT) | 0.054 | min-1 | With 15 mM Clâ» addition (38% increase) |
| âąOH Radical Contribution | 61.5 | % | Relative contribution to CT degradation |
| SOââąâ» Radical Contribution | 12.8 | % | Relative contribution to CT degradation |
| Direct Electron Transfer (DET) | 15 | % | Relative contribution to CT degradation |
| Steady-State [âąOH] Concentration | 3.2 x 10-13 | M | Estimated concentration |
| Steady-State [SOââąâ»] Concentration | 5.8 x 10-14 | M | Estimated concentration |
Key Methodologies
Section titled âKey MethodologiesâThe electrochemical degradation was performed under galvanostatic control in an undivided cell at ambient temperature.
- Electrode Setup: A BDD wafer (3.8 cm2 exposed area, 2.5-3 ”m thick film on Si) was used as the working anode. A Platinum foil (2 cm2) served as the counter electrode, and an Ag/AgCl (saturated KCl) electrode was the reference.
- Electrolyte Composition: 250 mL of electrolyte solution containing 40 ”M Cartap (CT) was used, supported by 0.05 M NaâSOâ.
- Operating Conditions: The solution pH was maintained at 3 (controlled by 1 M HâSOâ or 1 M NaOH). The temperature was ambient (22 °C).
- Current Application: Experiments were conducted under galvanostatic control with current densities ranging from 10 to 40 mA cm-2.
- Kinetic Analysis: The degradation kinetics were determined by measuring the remaining CT concentration using the DTNB procedure and UV-Vis spectrophotometry (412 nm).
- Radical Scavenging: Tert-butanol (TBA) and methanol (MeOH) were used as radical scavengers to quantify the relative contributions of âąOH and SOââąâ» radicals.
6CCVD Solutions & Capabilities
Section titled â6CCVD Solutions & CapabilitiesâThis research demonstrates the superior performance of Boron-Doped Diamond (BDD) electrodes for generating highly oxidative species essential for environmental remediation. 6CCVD is uniquely positioned to supply the high-specification BDD materials required to replicate, scale, and advance this research.
Applicable Materials
Section titled âApplicable MaterialsâTo achieve the high conductivity and stability required for efficient electrochemical AOPs, the following 6CCVD material is recommended:
- Heavy Boron-Doped PCD (Polycrystalline Diamond): The paperâs EDX analysis showed an exceptionally high boron concentration (15.1% B), indicating a need for heavy doping to minimize charge transfer resistance (RCT = 92.6 Ω). 6CCVD specializes in producing highly conductive BDD films, ideal for high-current-density applications like this electrochemical reactor.
- PCD Thickness and Substrate: The paper utilized a thin film (2.5-3 ”m) on a Si substrate. 6CCVD offers PCD films ranging from 0.1 ”m up to 500 ”m, allowing researchers to optimize film thickness for longevity and cost efficiency on standard Si or other custom substrates.
Customization Potential
Section titled âCustomization PotentialâThe experimental setup utilized specific electrode dimensions and materials (BDD anode, Pt cathode, Ag/AgCl reference). 6CCVD offers comprehensive customization services to meet precise engineering requirements:
| Research Requirement | 6CCVD Customization Capability | Value Proposition |
|---|---|---|
| Electrode Dimensions | Plates/wafers up to 125 mm (PCD/BDD). | Scale-up from the 3.8 cm2 lab-scale electrode to pilot or industrial reactor sizes. |
| Film Thickness | SCD/PCD films from 0.1 ”m to 500 ”m. | Precise control over BDD layer thickness for optimized conductivity and material cost management. |
| Metalization | Custom internal metalization (Au, Pt, Pd, Ti, W, Cu). | We can deposit custom contact layers (e.g., Ti/Pt/Au) or provide pre-metalized electrodes for simplified integration into electrochemical cells. |
| Surface Finish | Polishing services available (Ra < 5 nm for inch-size PCD). | While this application is kinetic, 6CCVD can provide ultra-smooth surfaces for applications requiring low friction or high optical quality. |
Engineering Support
Section titled âEngineering SupportâThe successful degradation of Cartap relies heavily on the precise generation of âąOH and SOââąâ» radicals, which is highly sensitive to BDD quality and doping level.
- AOP Optimization: 6CCVDâs in-house PhD team can assist researchers and engineers in selecting the optimal BDD material specifications (doping concentration, thickness, and surface morphology) for similar Electrochemical Advanced Oxidation Processes (AOPs) targeting refractory organic pollutants.
- Global Supply Chain: We offer reliable global shipping (DDU default, DDP available) to ensure timely delivery of custom diamond materials worldwide, supporting continuous research and development efforts.
For custom specifications or material consultation, visit 6ccvd.com or contact our engineering team directly.
View Original Abstract
In this work, the kinetic electrochemical degradation of Cartap (CT) (in Padan 95 SP) at boron-doped diamond (BDD) electrode was investigated. This study indicated that the degradation of CT underwent both direct and indirect oxidations. Water matrices can either accelerate or inhibit the removal efficiency of CT: adding 15 mM Cl<sup>-</sup> improved <i>k</i><i><sub>CT</sub></i> from 0.039 min<sup>-1</sup> to 0.054 min<sup>-1</sup> (increased by 38%), while <i>k</i><i><sub>CT</sub></i> decreased by 61.5% and 64% when increasing the concentration of HCO<sub>3</sub><sup>-</sup> and humic acid (HA) to 15 mM and 15 mg L<sup>-1</sup>, respectively. CT degradation was inhibited in the presence of methanol (MeOH) and <i>tert</i>-butanol (TBA) due to the scavenging effect of those chemicals toward reactive species. The contribution of reactive oxidants was calculated as: DET (direct electron transfer) accounted for 15%; âąOH accounted for 61.5%; SO<sub>4</sub><sup>âą-</sup> accounted for 12.8%; ROS (the other reactive oxygen species) accounted for 8.5%. The transformation pathways of major reactive species were established.