Study of carbon dioxide electrochemical reduction in flow cell system using copper modified boron-doped diamond
At a Glance
Section titled âAt a Glanceâ| Metadata | Details |
|---|---|
| Publication Date | 2020-01-01 |
| Journal | E3S Web of Conferences |
| Authors | Salsabila Zahran Ilyasa, Prastika Krisma Jiwanti, Munawar Khalil, Yasuaki Einaga, Tribidasari A. Ivandini |
| Institutions | University of Indonesia, Airlangga University |
| Citations | 4 |
| Analysis | Full AI Review Included |
Technical Documentation & Analysis: Copper-Modified BDD for COâ Reduction
Section titled âTechnical Documentation & Analysis: Copper-Modified BDD for COâ ReductionâThis document analyzes the research on using copper-modified boron-doped diamond (Cu-BDD) electrodes in a flow cell system for COâ electrochemical reduction (COâRR). It highlights the technical achievements and connects the material requirements directly to 6CCVDâs advanced MPCVD diamond capabilities.
Executive Summary
Section titled âExecutive SummaryâThe study successfully demonstrates the enhanced catalytic performance of Boron-Doped Diamond (BDD) electrodes modified with copper nanoparticles for COâ reduction, achieving high selectivity for formic acid (HCOOH) in a flow cell system.
- Material Enhancement: BDD electrodes were modified via chronoamperometry to deposit copper nanoparticles, significantly improving the catalytic activity compared to bare BDD.
- Optimal Configuration: The Cu-BDD 100s electrode, characterized by uniformly distributed Cu particles (~148 nm), was identified as the optimal configuration for COâRR.
- System Design: A two-compartment PTFE flow cell was utilized to enhance COâ mass transport, which is critical for high-efficiency electrochemical processes.
- Primary Product Selectivity: The flow cell system, combined with the Cu-BDD catalyst, selectively produced formic acid (HCOOH) as the main product.
- Performance Metric: The optimized Cu-BDD electrode achieved a Faradaic Efficiency (FE) of 33.00% for formic acid, more than doubling the efficiency of the bare BDD electrode (14.69% FE).
- Flow Cell Advantage: The use of the flow cell suppressed the formation of Câ/Câ hydrocarbon products, demonstrating the importance of system engineering in product selectivity.
Technical Specifications
Section titled âTechnical SpecificationsâThe following hard data points were extracted from the experimental results, focusing on the optimal Cu-BDD 100s electrode performance.
| Parameter | Value | Unit | Context |
|---|---|---|---|
| Base Electrode Material | Boron-Doped Diamond (BDD) | N/A | Prepared on Si(100) via MPCVD |
| Working Electrode Area | 9.62 | cm2 | Used in two-compartment PTFE flow cell |
| Optimal Cu Deposition Potential | -0.6 | V (vs. Ag/AgCl) | Chronoamperometry technique |
| Optimal Cu Deposition Time | 100 | seconds | Yielded Cu-BDD 100s electrode |
| Average Cu Particle Size | ~148 | nm | Observed via SEM on Cu-BDD 100s |
| Applied Reduction Potential | -1.5 | V (vs. Ag/AgCl) | Applied for 1 hour COâ reduction |
| COâ/Nâ Flow Rate | 200 | sccm | Gas bubbling rate into catholyte |
| HCOOH Faradaic Efficiency (Cu-BDD) | 33.00 | % | Highest selectivity achieved |
| HCOOH Concentration (Cu-BDD) | 11.33 | mg/L | Concentration of main liquid product |
| Hâ Faradaic Efficiency (Cu-BDD) | 21.25 | % | Competing hydrogen evolution reaction |
| Cu Mass Percentage (Optimal) | 0.83 | % | Determined by EDS on Cu-BDD 100s |
Key Methodologies
Section titled âKey MethodologiesâThe following steps outline the preparation of the BDD electrodes and the subsequent COâ electrochemical reduction process.
- BDD Substrate Growth: Boron-doped diamond films were prepared on Si(100) wafers using a Microwave Plasma-Assisted Chemical Vapor Deposition (MPCVD) system.
- Copper Electrodeposition: Copper modification was performed using a chronoamperometric technique in a solution of 1 mM CuSO4 in 0.1 M H2SO4.
- Potential Application: A constant potential of -0.6 V (vs. Ag/AgCl) was applied to the BDD working electrode for varying durations (25s, 50s, 100s, 150s) to optimize Cu loading.
- Electrode Characterization: Electrodes were analyzed using Scanning Electron Microscopy (SEM), Energy Dispersive X-ray analysis (EDX), and X-Ray Photoelectron Spectroscopy (XPS) to confirm Cu deposition and uniformity.
- Flow Cell Setup: COâ reduction was carried out in a two-compartment PTFE flow cell separated by a Nafion membrane. The working electrode was Cu-BDD, with Ag/AgCl as the reference and Pt plate as the counter electrode.
- Electrolysis Procedure: The catholyte was saturated first with Nâ (30 minutes) and then with COâ (15 minutes) at 200 sccm. Reduction was performed for 1 hour at -1.5 V.
- Product Quantification: Liquid products (HCOOH) were analyzed using High-Performance Liquid Chromatography (HPLC), and gaseous products (CO, CHâ, Hâ) were analyzed using Gas Chromatography (GC).
6CCVD Solutions & Capabilities
Section titled â6CCVD Solutions & CapabilitiesâThis research validates the critical role of high-quality Boron-Doped Diamond (BDD) substrates in advanced electrochemical applications like COâ reduction. 6CCVD is uniquely positioned to supply and enhance the materials required to replicate and scale this research.
| Research Requirement | 6CCVD Solution & Capability | Technical Advantage & Sales Driver |
|---|---|---|
| Applicable Materials: High-Quality BDD Substrates | Heavy Boron-Doped PCD/SCD Wafers. We supply MPCVD-grown BDD materials with controlled boron doping levels necessary for wide potential window electrochemistry and high stability. | Our BDD materials ensure low background current and superior chemical inertness, maximizing the efficiency of the Cu active sites. We offer both Polycrystalline (PCD) and Single Crystal (SCD) BDD options. |
| Electrode Dimensions: 9.62 cm2 Working Area | Custom Dimensions & Precision Laser Cutting. 6CCVD manufactures PCD plates up to 125mm diameter. We provide precision laser cutting services to match exact flow cell geometries (e.g., 9.62 cm2) or custom shapes required for scale-up. | Engineers can specify exact dimensions, eliminating material waste and ensuring perfect integration into proprietary flow cell or reactor designs. |
| Surface Modification: Uniform Cu Nanoparticle Deposition | Integrated Metalization Services (Cu, Pt, Pd, Ti). While the paper used electrodeposition, 6CCVD offers advanced, high-uniformity metal deposition (e.g., sputtering or evaporation) of Cu, Pt, or Pd layers directly onto the BDD surface. | Achieve superior adhesion, purity, and thickness control of the catalytic layer, potentially leading to more stable and reproducible Faradaic Efficiencies than simple electrochemical methods. |
| Surface Finish: Requirement for uniform nucleation | Ultra-Low Roughness Polishing. Our standard polishing achieves Ra < 5 nm for inch-size PCD and Ra < 1 nm for SCD. A pristine, low-roughness surface is crucial for controlled, uniform nucleation of metal nanoparticles. | A smoother surface minimizes defects and ensures predictable electrodeposition kinetics, maximizing the density and uniformity of the catalytic Cu sites. |
| Engineering Support: Optimization for COâRR | In-House PhD Engineering Team. 6CCVD provides consultation on material selection, doping concentration, and surface termination (e.g., hydrogen vs. oxygen termination) to optimize BDD performance for specific COâRR products (e.g., HCOOH, CO, or Câ species). | Leverage our expertise to accelerate your research timeline and ensure the diamond substrate is perfectly tailored for your specific electrochemical application. |
For custom specifications or material consultation, visit 6ccvd.com or contact our engineering team directly.
View Original Abstract
High concentrations of CO2 in the atmosphere may cause climate and environmental changes. Therefore, various research has been extensively performed to reduce CO 2 by converting CO 2 directly into hydrocarbons. In this research, CO 2 electrochemical reduction was studied using boron-doped diamond (BDD) modified with copper nanoparticles to improve BDD electrodesâ catalytic properties. The deposition was performed by chronoamperometry technique at a potential of -0.6 V (vs. Ag/AgCl) and characterized using SEM, EDS, XPS, and cyclic voltammetry (CV). CO 2 electrochemical reduction on BDD and Cu-BDD was carried out at -1.5 V (vs. Ag/AgCl) for 60 minutes. The products were analyzed using HPLC and GC. The product was mainly formic acid with a concentration of 11.33 mg/L and 33% faradaic efficiency on a Cu-BDD electrode.