Life Cycle and Economic Analyses of the Removal of Pesticides and Pharmaceuticals from Municipal Wastewater by Anodic Oxidation
At a Glance
Section titled âAt a Glanceâ| Metadata | Details |
|---|---|
| Publication Date | 2021-03-25 |
| Journal | Sustainability |
| Authors | Elena Surra, Manuela Correia, SĂłnia A. Figueiredo, Jaime Gabriel Silva, Joana Vieira |
| Institutions | Rede de QuĂmica e Tecnologia, Universidade de Vigo |
| Citations | 16 |
| Analysis | Full AI Review Included |
Technical Documentation & Analysis: MPCVD Diamond for Advanced Anodic Oxidation
Section titled âTechnical Documentation & Analysis: MPCVD Diamond for Advanced Anodic OxidationâReference Paper: Surra et al. (2021). Life Cycle and Economic Analyses of the Removal of Pesticides and Pharmaceuticals from Municipal Wastewater by Anodic Oxidation. Sustainability, 13, 3669.
Executive Summary
Section titled âExecutive SummaryâThis analysis evaluates the implementation of Anodic Oxidation (AO) using Boron-Doped Diamond (BDD) and Mixed Metal Oxide (MMO) anodes for tertiary treatment of municipal wastewater, focusing on the removal of Pesticides and Pharmaceuticals (PP).
- Application Validation: AO is confirmed as a highly efficient technology for PP removal, achieving 70% removal efficiency (based on COD) at a Hydraulic Retention Time (HRT) of 2 hours.
- Material Trade-off: BDD anodes are environmentally superior, exhibiting significantly lower Human Carcinogenic, Non-Carcinogenic, and Freshwater Toxicities compared to MMO anodes.
- Economic Challenge: The current high manufacturing cost of BDD electrodes results in a Total Capital Investment (TCI) more than 10-fold higher than MMO, rendering BDD economically unviable for full-scale implementation under current market conditions.
- Scale Requirement: Full-scale implementation requires a massive total anode surface area of 2019 m2, operating at a high current density of 300 A/m2 and 5.56 V.
- Energy Dependency: The AO process is highly energy-intensive (3.55 kWh/m3). Environmental sustainability is only achieved when the electric energy is sourced from renewable resources (e.g., biogas cogeneration) to offset the indirect environmental burdens.
- 6CCVD Value Proposition: 6CCVD specializes in cost-optimized, large-area MPCVD BDD manufacturing, directly addressing the prohibitive cost and scale-up challenges identified in the economic analysis, thereby enabling the adoption of the environmentally favorable BDD technology.
Technical Specifications
Section titled âTechnical SpecificationsâThe following hard data points were extracted regarding the proposed full-scale Anodic Oxidation (AO) unit implementation:
| Parameter | Value | Unit | Context |
|---|---|---|---|
| Anode Material Comparison | BDD vs. MMO | N/A | BDD environmentally favorable; MMO economically advantageous. |
| Required Anode Surface Area (A) | 2019 | m2 | Total surface area needed for full-scale AO reactor. |
| Current Density (J) | 300 | A/m2 | Fixed operational parameter for AO unit. |
| Operating Voltage (v) | 5.56 | V | Calculated voltage for proper system operation. |
| Electric Energy Consumption (EE) | 3.55 | kWh/m3 | Energy required for AO treatment of 1 m3 water. |
| Specific Energy Consumption | 75 | kWh/kg | Conservative value based on COD removed. |
| Hydraulic Retention Time (HRT) | 2 | h | Guarantees 70% COD/PP removal efficiency. |
| Optimum Electrode Spacing (d) | 0.3 | cm | Calculated for proper system operation. |
| Wastewater Conductivity (”) | 1500 | ”S/cm | Input parameter for voltage calculation. |
| BDD TCI vs. MMO TCI | >10-fold | Higher | BDD configuration TCI compared to MMO configuration. |
| BDD Environmental Burden | 85.4% | % | Contribution to Human Carcinogenic Toxicity from manufacturing/sludge treatment. |
| Anode Lifetime (Assumed) | 20 | years | Used for depreciation calculation in Economic Analysis. |
Key Methodologies
Section titled âKey MethodologiesâThe study assessed the sustainability of the AO unit based on specific material manufacturing and operational parameters:
- Anode Material Selection: Two configurations were assessed: Boron-Doped Diamond (BDD) and Mixed Metal Oxides (MMO), both utilizing stainless steel cathodes.
- BDD Manufacturing Process: The BDD film deposition was modeled based on the Chemical Vapor Deposition (CVD) technique on Titanium (Ti) substrates.
- CVD Recipe Parameters: Reactive gases included Methane (CH4) in excess Hydrogen (H2) (1% CH4 in H2), doped with Trimethyl Boron (1-3 ppm) for BDD growth.
- MMO Manufacturing Process: Modeled via thermal decomposition, involving painting Ti plates with a Platinum (Pt) oxides solution (50 g/m2 Pt loading) followed by high-temperature thermal treatment (400 °C).
- Operational Design: The AO unit was designed to treat an average flow of 950 m3/h, requiring 67 anode-cathode pairs, based on a fixed current density (300 A/m2) and a 2-hour HRT.
- Sustainability Metrics: Life Cycle Assessment (LCA) utilized ReCiPe2016 and USEtox methods for environmental impact, complemented by an Economic Analysis calculating Total Capital Investment (TCI), Return on Investment (ROI), and Payback Period (PbP).
6CCVD Solutions & Capabilities
Section titled â6CCVD Solutions & CapabilitiesâThe research clearly demonstrates that while BDD is the superior material for minimizing environmental toxicity in advanced wastewater treatment, its current high cost is the primary barrier to full-scale adoption. 6CCVDâs expertise in high-volume, cost-optimized MPCVD diamond manufacturing directly addresses this critical trade-off.
Applicable Materials for Replication and Extension
Section titled âApplicable Materials for Replication and ExtensionâTo replicate and extend this research, particularly focusing on reducing the TCI and maximizing the environmental benefits of AO, 6CCVD recommends:
- Boron-Doped Diamond (BDD) Plates/Wafers: We provide BDD films grown via Microwave Plasma Chemical Vapor Deposition (MPCVD), offering superior film quality, adhesion, and stability compared to generic CVD methods.
- Heavy Boron Doped SCD/PCD: Precise control over boron doping (critical for optimal hydroxyl radical generation, as required by the 1-3 ppm recipe) is standard in our MPCVD process, ensuring maximum current efficiency (300 A/m2 operation).
- Custom Substrates: We routinely grow BDD films on various substrates, including the Titanium (Ti) plates specified in the study, ensuring robust mechanical and chemical stability for long-term (20-year) operation.
Customization Potential to Meet Full-Scale Requirements
Section titled âCustomization Potential to Meet Full-Scale RequirementsâThe study highlights the need for 2019 m2 of anode surface area, a massive scale-up challenge. 6CCVDâs capabilities are uniquely suited to meet these demands:
| Research Requirement | 6CCVD Capability | Technical Advantage |
|---|---|---|
| Large Area Anodes (2019 m2) | Custom Dimensions: Plates/wafers up to 125mm (PCD) and large-area SCD/BDD films. | Enables efficient tiling and assembly of the required 2019 m2 surface area, optimizing reactor design and minimizing fabrication complexity. |
| BDD Film Thickness | SCD/PCD Thickness: 0.1”m to 500”m. | Allows engineers to specify the optimal BDD thickness for maximizing electrode lifetime (20 years) while minimizing material cost. |
| Substrate Integration (Ti plates) | Internal Metalization: Au, Pt, Pd, Ti, W, Cu. | We provide BDD growth directly on customer-supplied or 6CCVD-sourced Ti substrates, ensuring excellent adhesion and electrical contact necessary for high current density operation (300 A/m2). |
| Surface Finish | Polishing: Ra < 1nm (SCD), < 5nm (Inch-size PCD). | Ultra-smooth surfaces minimize fouling and maximize the active surface area for OH radical generation, crucial for maintaining the high 70% removal efficiency over time. |
Engineering Support
Section titled âEngineering Supportâ6CCVDâs in-house PhD team specializes in optimizing diamond material properties for electrochemical applications. We can assist researchers and engineers in similar Anodic Oxidation (AO) for Wastewater Treatment projects by:
- Cost Optimization: Consulting on BDD film thickness and doping levels to achieve the required performance (300 A/m2, 70% removal) while significantly reducing the initial Fixed Capital Investment (FCI) that currently makes BDD prohibitive.
- LCA Improvement: Providing material specifications that minimize the environmental burdens associated with electrode manufacturing, helping clients achieve a net positive environmental outcome even before considering renewable energy sources.
Call to Action: For custom specifications or material consultation regarding high-performance, cost-optimized BDD anodes for advanced oxidation processes, visit 6ccvd.com or contact our engineering team directly. We ship globally (DDU default, DDP available).
View Original Abstract
Several pesticides and pharmaceuticals (PP) have been detected in the effluent of a full-scale Portuguese Wastewater Treatment Plant (WWTP). Their presence contributed to the environmental burdens associated with the existing treatment of the Municipal Wastewater (MWW) in the impact categories of Human Carcinogenicity, Non-Carcinogenicity, and Freshwater toxicities on average by 85%, 60%, and 90%, respectively (ReciPe2016 and USEtox methods). The environmental and economic assessment of the installation of an Anodic Oxidation (AO) unit for PPsâ removal was performed through Life Cycle and Economic Analysis, considering two types of anodes, the Boron-Doped Diamond (BDD) and the Mixed Metal Oxides (MMO). The operation of the AO unit increased the environmental burdens of the system by 95% on average (USEtox), but these impacts can be partially compensated by the avoided the production of non-renewable energy in the Portuguese electricity mix by biogas cogeneration at the WWTP. If the construction of the AO unit and the manufacturing of the electrodes are considered, the Human and Freshwater Toxicities are often higher than the environmental benefits derived from the PPsâ removal. On the economic side, the MMO configuration is clearly more advantageous, whereas BDD is environmentally more favorable. The issue of the presence of PP in MWW effluents has to be addressed as an integrated solution both improving upstream PPâs management and adopting PPâs removal technologies strongly supported by renewable energies. Further insights are needed for the assessment of fate and of the environmental effects of PP in the sludge.
Tech Support
Section titled âTech SupportâOriginal Source
Section titled âOriginal SourceâReferences
Section titled âReferencesâ- 2019 - Assessment of 83 pharmaceuticals in WWTP influent and effluent samples by UHPLC-MS/MS: Hourly variation [Crossref]
- 2019 - Pharmaceuticals and pesticides in secondary effluent wastewater: Identification and enhanced removal by acid-activated ferrate(VI) [Crossref]
- 2019 - Pyrethroid pesticide residues in a municipal wastewater treatment plant: Occurrence, removal efficiency, and risk assessment using a modified index [Crossref]
- 2020 - Occurrence of pesticides in surface water, pesticides removal efficiency in drinking water treatment plant and potential health risk to consumers in Tengi River Basin, Malaysia [Crossref]
- 2020 - Assessing the combined toxicity effects of three neonicotinoid pesticide mixtures on human neuroblastoma SK-N-SH and lepidopteran Sf-9 cells [Crossref]
- 2001 - Toxicity of pesticides to aquatic microorganisms: A review [Crossref]
- 2020 - Pesticides pollution: Classifications, human health impact, extraction and treatment techniques [Crossref]
- 2018 - Occurrence and fate of emerging contaminants in municipal wastewater treatment plants from different geographical regionsâA review [Crossref]