Design and Application of Hetero-Multicomponent Metal Oxide Photocatalysts for Wastewater Treatment: Ti–Cu–Zn Catalysts and Future Research Directions
Abstract
1. Introduction
2. Advanced Oxidation Processes in Wastewater Treatment
3. Sandwiched Nanostructures: Design Principles
3.1. Design Principles and Applications
3.1.1. Material Selection and Layering
3.1.2. Synergistic Effects
3.1.3. Structural Design and Stability
3.1.4. Biomimetic and Flexible Designs
4. Ti–Cu–Zn Nanostructures: Properties and Photocatalytic Behavior
4.1. Properties of Ti–Cu–Zn Nanostructures
4.1.1. Structural and Morphological Properties
4.1.2. Optical and Electronic Properties
4.1.3. Chemical and Thermal Properties
4.2. Photocatalytic Behavior in Wastewater Treatment
4.2.1. Mechanism of Photocatalysis
- Light Absorption: The nanocomposite absorbs light, generating electron–hole pairs.
- Charge Separation: The heterojunctions between TiO2, ZnO, and CuO facilitate charge separation, reducing recombination.
4.2.2. Degradation Efficiency
- Rhodamine B Degradation: A degradation efficiency of 96.1% is reported for CuO–ZnO nanocomposites under optimized conditions [64].
4.2.3. Active Species and Stability
4.3. Synthesis Methods
Overview of Synthesis Techniques
4.4. Applications in Wastewater Treatment
4.4.1. Target Pollutants
- Phenols: The nanocomposites achieve significant phenol removal under solar irradiation with rates between 54% and 80% [71].
- Azo Dyes: High degradation efficiency for azo dyes is reported, with rate constants exceeding 0.04 min−1 [70].
- Pesticides: Imidacloprid is completely mineralized (~100%) under solar-simulated light with efficiency above 91% after multiple reuse cycles [85].
- Herbicides: 2,4-dichlorophenol (2,4-DCP) and related chlorophenols achieve ~92% TOC mineralization using nanostructures under visible light [86].
- Fertilizers (nitrate, ammonia nitrogen): Photocatalytic systems have demonstrated notable performance in fertilizer-related wastewater treatment. Complete nitrate removal with approximately 70% selective conversion to ammonium under UV light [87], while 61% of ammonia-nitrogen was degraded within 3 h, retaining 52% efficiency after three reuse cycles [88].
4.4.2. Antibacterial Activity
4.4.3. Comparative Photocatalytic Performance of TiO2-Based Systems Against Key Contaminants
5. Mechanistic Insights into Photocatalytic AOPs
- TiO2 absorbs light → e− + h+ generation
- e− transfer to Cu2+ → Cu+ and •O2−
- h+ reacts with H2O/OH− → •OH
- •O2− and •OH and degrade pollutants
- The surface sites of Zn2+ stabilize charges and inhibit recombination
Strengths and Limitations of Ti–Cu–Zn Systems Compared to Single/Bimetallic Systems
6. Stability, Reusability, and Environmental Safety
6.1. Coating Durability on Steel Substrates
6.2. Photo-Corrosion Resistance and Structural Integrity
6.3. Catalyst Reusability
6.4. Leaching Behavior and Ecotoxicological Impact
7. Engineering Considerations and Scale-Up Potential
7.1. Integration into Decentralized Treatment Units
7.2. Reactor Design and Light Penetration Efficiency
7.3. Cost and Scalability of Synthesis
7.4. Performance in Complex Wastewater Matrices
7.5. Automation, Monitoring, and Maintenance
7.6. Sustainability Considerations
7.7. Commercialization and Market Potential
7.8. Regulatory & Deployment Checklist for Agricultural Use
8. Future Perspectives and Research Opportunities
- Tailored band engineering using advanced dopants or quantum heterostructures to expand light absorption into the near-infrared region and enhance charge carrier lifetimes.
- Hybrid integration of AOP, such as coupling heterocatalysts with ozonation, Fenton, or electrochemical oxidation, to boost degradation efficiency.
- Real-time contaminant monitoring technologies combined with intelligent photocatalyst systems for adaptive water treatment.
- Green and scalable synthesis methods that eliminate toxic solvents, reduce energy input, and enable on-site fabrication.
- Ecotoxicity and life cycle assessment (LCA) studies to ensure safe deployment in agricultural, municipal, and industrial settings.
- Furthermore, fundamental studies on catalyst-pollutant interaction kinetics and reactive intermediate tracking will be vital for mechanism elucidation and rational catalyst design.
Knowledge Gaps and Future Perspectives
- Need for in situ characterization techniques: Current studies often rely on post-reaction analyses. Incorporating in situ techniques (e.g., X-ray Photoelectron Spectroscopy (XPS), Diffuse Reflectance Infrared Fourier Transform Spectroscopy (DRIFTS), and Electron Paramagnetic Resonance (EPR) under operational conditions) would help track the dynamics of charge transfer, surface species, and ROS generation.
- Reusability and stability studies: Current studies have no experiments on reusability and stability, and therefore, new studies going forward have to focus on this. Ensuring that the synthesized catalyst can achieve nothing less than 15% degeneration after 5 runs will be a huge win for the system, as this is the minimal requirement seen in other single or binary catalyst systems.
- Heavy metal reduction: Industrial, pharmaceutical, and agricultural wastewater systems tend to contain heavy metals such as chromium, cadmium, lead, etc. More studies must be carried out on the efficiency of removing these heavy metals from wastewater, as current studies do not have citable references for these elements.
- Exploring new dopants and structural motifs: Beyond Cu and Zn, incorporation of rare earth, non-metal (e.g., N, S), or perovskite-inspired interfaces may further tune band alignment and enhance activity.
- Policy and regulatory alignment: For field deployment, regulatory clarity is required regarding nanoparticle release, reuse standards, and permissible leaching thresholds. Engagement with environmental authorities, farmers, and policymakers is essential to facilitate technology transfer.
9. Conclusions
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Acknowledgments
Conflicts of Interest
References
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| Property | Typical Range | Functionality | References |
|---|---|---|---|
| Band gap | 2.2–3.3 eV | Controls light absorption | Taufik et al., 2017 [61] |
| Surface area | 60–120 m2/g | More active sites for degradation | Taufik et al., 2017 [61] |
| Crystalline phases | Anatase (TiO2), Monoclinic (CuO), Wurtzite (ZnO) | Phase synergy | Kumar et al., 2017 [68] |
| Morphology | Spherical, rod-shaped, agglomerated | Affects light harvesting | Yitagesu et al., 2024 [67] |
| Synthesis Method | Description | Pros | Cons | References |
|---|---|---|---|---|
| Sol–Gel Method | Produces uniform nanocomposites with high surface areas and tailored band gaps. | Simple equipment, fine compositional control, homogeneous mixing of precursors. | Long processing times, potential for cracking during drying/calcination. | Taufik et al., 2017 [61] Albert et al., 2015 [62] Baig et al., 2024 [70] |
| Hydrothermal Method | Uses high-temperature, high-pressure aqueous conditions to control particle size and morphology. | Excellent control over crystal growth, high purity, and energy efficiency for certain systems. | Requires an autoclave, limited scalability for industrial production. | Malakootian et al., 2021 [60] Nassar et al., 2024 [66] Kumar et al., 2017 [68] |
| Biosynthesis | Employs plant extracts as reducing/stabilizing agents for green synthesis. | Eco-friendly, cost-effective, low-toxicity byproducts. | Batch-to-batch variability, limited control over particle size/shape. | Jeevarathinam et al., 2024 [64] Yitagesu et al., 2024 [67] |
| Mechanical Mixing and Wet Impregnation | Physically mixes powders or impregnates supports with precursors, followed by drying/calcination. | Low-cost, scalable, straightforward process. | Non-uniform distribution of active sites, possible agglomeration. | Mohammadi et al., 2016 [71] |
| Spray Pyrolysis | Aerosolized precursor solution is thermally decomposed to form thin films or powders. | Uniform film deposition, good for large-area coatings, compatible with dopants. | Requires specialized spray equipment and higher energy use. | Chen et al., 2022 [45] Mrabet et al., 2023 [80] |
| Gas-Phase Fabrication | Vapor-phase routes produce crystalline nanoparticles with minimal liquid waste. | High purity, excellent crystallinity, and a clean process. | High cost, requires advanced equipment and expertise. | Hudandini et al., 2024 [81] |
| Pollutant | Catalyst System | Light Source | Degradation Efficiency (%) | Time (min) |
|---|---|---|---|---|
| Methylene Blue | TiO2 [89] | UV | 62.72 | 120 |
| TiO2–CuO [90] | UV | 92.31 | 120 | |
| TiO2–ZnO [91] | UV | 96.4 | 720 | |
| Ti–Cu–Zn [61] | UV | 100 | 120 | |
| Heavy metal | TiO2 [92] | Visible | 88 | 120 |
| TiO2–CuO [93] | Visible | 95 | 45 | |
| TiO2–ZnO [94] | Visible | 53 | 288 | |
| Ti–Cu–Zn | - | - | - | |
| Bacteria | TiO2 [28] | UV | 100 | 10 |
| TiO2–CuO [95] | Visible | 98 | 60 | |
| TiO2–ZnO [96] | UV | 98 | 30 | |
| Ti–Cu–Zn [68] | Visible | 99 | 30–120 |
| System | Strengths | Limitations | References |
|---|---|---|---|
| TiO2 only | Highly stable, inexpensive, well-known, safe in most environments | UV-only activity, high recombination, limited ROS production | Ghamarpoor et al., 2024 [105] |
| TiO2–CuO | Enhanced visible-light activity, better charge separation, Schottky junction promote electron migration. | Cu2+ leaching risk; CuO instability in repeated cycles; poor scalability | Shi et al., 2019 [106], A’srai et al., 2023 [107] |
| TiO2–ZnO | Stronger ROS production; antibacterial synergy; better charge migration | Wide band gap (3.3 eV); ZnO is prone to photo corrosion in aqueous systems | Ghamarpoor et al., 2024 [105], Kubiak et al., 2019 [108] |
| Ti–Cu–Zn | Combined broad-spectrum light response; superior ROS; dual action (degradation + antibacterial); lower e−/h+ recombination | Still under development; leaching of Cu/Zn and durability under real water conditions remain concerns | Malakootian et al., 2021 [60], Taufik et al., 2017 [61], Mohammadi et al., 2016 [71], Abdelfattah and El-Shamy, 2024 [109] |
| Environmental Safety: Ti–Cu–Zn | Effective pollutant degradation with reduced chemical inputs; no need for chemical oxidants; low toxicity at moderate loading | Requires leachate testing and chronic toxicity assessments (Cu/Zn risk); reusability beyond 5 cycles is underexplored | Abdelfattah and El-Shamy., 2024 [109], Joonas et al., 2019 [110], Azizi-lalabadi et al., 2019 [111] |
| Criteria | Current Status | Recommendation |
|---|---|---|
| Leaching Safety (Cu/Zn) | Partial data | Add bioassays (e.g., Daphnia, algal tests) |
| Catalyst Reuse Data | <5 cycles reported | Target ≥10 with <15% performance loss |
| Field Testing | Rare | Needed in realistic Agri-runoff systems |
| Policy Guidelines | Lacking | Propose collaboration with local agencies |
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Onoriode-Afunezie, M.-A.O.; Krutkevičius, J.; Šulčiūtė, A. Design and Application of Hetero-Multicomponent Metal Oxide Photocatalysts for Wastewater Treatment: Ti–Cu–Zn Catalysts and Future Research Directions. Molecules 2026, 31, 299. https://doi.org/10.3390/molecules31020299
Onoriode-Afunezie M-AO, Krutkevičius J, Šulčiūtė A. Design and Application of Hetero-Multicomponent Metal Oxide Photocatalysts for Wastewater Treatment: Ti–Cu–Zn Catalysts and Future Research Directions. Molecules. 2026; 31(2):299. https://doi.org/10.3390/molecules31020299
Chicago/Turabian StyleOnoriode-Afunezie, Maria-Anthoniette Oghenetejiro, Justinas Krutkevičius, and Agnė Šulčiūtė. 2026. "Design and Application of Hetero-Multicomponent Metal Oxide Photocatalysts for Wastewater Treatment: Ti–Cu–Zn Catalysts and Future Research Directions" Molecules 31, no. 2: 299. https://doi.org/10.3390/molecules31020299
APA StyleOnoriode-Afunezie, M.-A. O., Krutkevičius, J., & Šulčiūtė, A. (2026). Design and Application of Hetero-Multicomponent Metal Oxide Photocatalysts for Wastewater Treatment: Ti–Cu–Zn Catalysts and Future Research Directions. Molecules, 31(2), 299. https://doi.org/10.3390/molecules31020299

