Research Progress on Novel Semiconductor Photocatalysts for Degrading VOCs
Abstract
1. Introduction
2. Standardized Evaluation Methods for Photocatalytic Efficiency
2.1. Standardization Strategies and the Proper Use of ζr
2.2. A Quality-Filtering Framework and Future Directions
3. TiO2-Based Catalysts
3.1. TiO2-Based Tier I Studies with Standardized Reporting
3.2. Ion Doping: Qualitative Trends from TiO2 Tier II Studies
3.3. Surface Modification: Qualitative Trends from TiO2 Tier II Studies
4. g-C3N4-Based Catalysts
4.1. g-C3N4-Based Tier I Studies with Standardized Reporting
4.2. Metal Decoration and Heterojunctions: Qualitative Trends from g-C3N4 Tier II Studies
5. Bismuth-Based Oxides
5.1. Bismuth-Based Tier I Studies with Standardized Reporting
5.2. Self-Doping and Microstructure: Qualitative Trends from Bismuth-Based Tier II Studies
6. Metal–Organic Frameworks (MOFs)
6.1. MOF-Based Tier I Studies with Standardized Reporting
6.2. Ligand Functionalization and Composites: Qualitative Trends from MOF-Based Tier II Studies
7. Conclusions
Author Contributions
Funding
Data Availability Statement
Conflicts of Interest
References
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| Catalyst (Modification) | Target VOC (Conc.) | Light Source | Photon Flux & Quantum Yield | Reactor Type | Ref. |
|---|---|---|---|---|---|
| Amorphous titania nanofilm (AM-RT) | Formaldehyde (54 ± 1 ppm) | UV lamp (254 nm) | Photon flux: 1.26 mW/cm2; AQY: 60.4% | Single-pass continuous flow | [17] |
| N-doped TiO2 (N/Ti = 1) | Formaldehyde (100 ppm) | UV-A (32 W lamp) | AQY: 1.72 × 10−2 molecules photon−1 | Packed-bed tubular | [18] |
| Na,Pd-modified TiO2 (Schottky + O vacancy) | Toluene (4 ppm) | 4 × 8 W UV lamps (λ_max = 254 nm, total 32 W) | Photon flux: 0.038 W (incident power on catalyst); AQY: 0.130% | Continuous flow (tubular fixed-bed) | [19] |
| ZnSn(OH)6/TiO2 S-scheme heterojunction (ZST) | Benzene (1 ppm) | UV-A LED (1 W, λ_max = 370 nm) | Photon flux: 0.0125 W/cm2; AQY: 6.08 × 10−3% | Portable (chamber, 24.5 L, circulating) | [20] |
| Pt/N-co-doped TiO2 (1 wt% Pt, N/Ti = 1) | Formaldehyde (200 ppm) | UV-A lamp (365 nm, 32 W) | AQY: 5.58% | Tubular fixed-bed (continuous flow) | [21] |
| Ag2O/TiO2 p-n S-scheme heterojunction (AT-4) | Benzene (1 ppm) | UV-A LED (λ_max = 352 nm, total 32 W, incident power 0.050 W) | Photon flux: 0.050 W; AQY: 0.061% | Continuous flow (tubular fixed-bed) | [22] |
| Alkalinized g-C3N4 (K-doped + OH-grafted + Fe3+) | Isopropanol | 300 W Xe lamp with cutoff filter (λ > 400 nm); AQY at 420 ± 16 nm | Photon flux: 0.45 mW/cm2; AQY: 49% at 420 nm | Batch (plate-type, solid–gas) | [23] |
| CeO2-TiO2/g-C3N4 ternary | Toluene | 4 × 6 W daylight (410–580 nm) + UV (~350 nm) | AQY: UV 12.5 × 10−4%, sunlight 3.1 × 10−4% | Batch (flat plate) | [24] |
| g-C3N4/TiO2 composite (CNT-0.02) | Formaldehyde (5 ppm) | Low-power UV-A LED (1 W, λ_max = 370 nm) | QY: 2.74 × 10−3 molecules photon−1 | Portable (chamber, 17 L, circulating) | [25] |
| Crystalline Bi2WO6 (russellite) | Acetaldehyde (2000 ppm) | Visible light (λ > 400 nm); action spectrum measured | AQY: 8% at 400 nm | Batch (gas–solid) | [26] |
| BiOCl with surface defects (BiOCl-R) | Toluene (5 ppm) | 4 × 8 W UV lamps (total 32 W) | Photon flux: 0.076 W (incident power on catalyst); QY: 1.04 × 10−3 molecules photon−1 | Continuous flow (tubular fixed-bed) | [27] |
| CeO2/Ce-MOF isogenous S-scheme heterojunction | Acetaldehyde (200 ppm) | 300 W Xe lamp with 420 nm cutoff filter; intensity 100 mW/cm2 | Photon flux: 100 mW/cm2; AQE: 7.15% at 420 nm | Batch (500 mL Tedlar bag) | [28] |
| Ag-WO3/NH2-MIL-125 MAH-S heterojunction (AWM-10) | Formaldehyde (5 ppm) | 1 W UV-LED (λ_max = 370 nm) | AQY: 0.238% | Portable (chamber, 17 L, circulating) | [29] |
| Catalyst (Modification) | Target VOC (Conc.) | Light Source (λ) | Reactor Type | Qualitative Observation (Within-Study Enhancement) | Ref. |
|---|---|---|---|---|---|
| Sn-doped NaYF4/Sn@TiO2 | Formaldehyde, TVOCs | 500 W xenon lamp | Sealed circulating chamber (1 m3) | Enhanced formaldehyde and TVOC removal compared to pure TiO2; improvement attributed to Sn doping and upconversion luminescence synergy | [30] |
| Graphene/S,N-co-doped TiO2 (0.1 wt% rGO/S0.05N0.1TiO2) | Formaldehyde (1 ppm) | Fluorescent lamp (10 W, 360–700 nm, peak 436 nm) | Continuous flow (pyrex tube coating) | Outperformed other tested compositions under fluorescent light; optimal at 20% RH; enhanced visible-light absorption and electron transfer due to S,N co-doping and graphene | [31] |
| W-doped TiO2 (0.5 wt%) | Toluene (10 ppm) | UV lamp (352 nm, 8 W) | Continuous flow (plug flow, coated on glass slides) | Highest degradation efficiency among W, Fe, Mn dopants under identical UV conditions; stable for extended operation | [32] |
| Oxygen-vacancy-enriched TiO2 (hydrothermally treated) | Toluene (20 ppm) | 300 W Xe lamp | Continuous flow (fixed-bed, glass slides) | Significantly higher removal and mineralization compared to P25; improved stability and lattice oxygen activation via water-driven Ti–O bond weakening | [33] |
| TiO2/hierarchical ZSM-5 (TZ-2) | Toluene (60 ppm) | 300 W Xe lamp (simulated sunlight) | Batch (500 mL, sealed) | Enhanced degradation compared to bare TiO2 and TiO2/commercial ZSM-5; Ti–O–Si bond formation narrows bandgap and improves charge separation | [34] |
| TiO2 quantum dots loaded on anatase TiO2 nanoparticles (TiO2-QD1) | Toluene (20 mg/m3) | 150 W UV lamp (254 nm) | Batch (sealed, 0.216 m3) | Higher reaction rate and mineralization efficiency than bare TiO2; QD loading induces upward band bending and promotes charge separation | [35] |
| Surface C-modified TiO2 (THF-50-TiO2) and surface CN-modified TiO2 (PY-1-TiO2) | Toluene (800 ppm) | 300 W high-pressure Hg lamp (UV) | Batch (300 mL, stainless steel) | Surface C or CN modification enhances charge separation and extends light absorption; both modified catalysts outperform unmodified TiO2, with CN doping enabling visible-light activity | [36] |
| Ni-modified g-C3N4 (0.1 wt% Ni) | Styrene (2 ppm) | Fluorescent lamp (10 W, visible, light intensity 36.5 μE/m2/s) | Continuous flow (annular photoreactor, catalyst coated on inner tube) | Ni acts as electron trap, suppressing recombination and enhancing charge separation; optimal Ni loading improves visible-light absorption and surface area | [37] |
| K-doped g-C3N4/BiOCl heterojunction (KCN1/BOC) | Toluene (30 ppm) | 350 W Xe lamp (simulated solar light) | Batch (Teflon bag, 2.5 L, quartz window) | K+ intercalation creates electron transfer channels; p-n heterojunction with Z-scheme enhances charge separation; main ROS are •O2− > •OH > h+ | [38] |
| CdS@g-C3N4 (0.2) (CdS nanoparticles on g-C3N4 via microwave-assisted sol–gel) | Gaseous toluene (200 ppm, 30% RH) | Visible light (20 W Xe lamp) | 500 mL homemade gas-phase photocatalytic reactor | Heterojunction broadens light absorption and improves charge separation, significantly outperforming pure CdS | [39] |
| AC@g-C3N4/MnOx (AC12.5%@g-C3N4/MnOx) (activated carbon, g-C3N4, and MnOx composite, Z-scheme heterojunction) | Acetaldehyde (3.5 mg/m3) | UV light (254 nm mercury lamp) | Continuous flow system (0.5 L/min, 50% RH, 20 °C) | Z-scheme mechanism enhances O2− generation; AC adsorption–photocatalysis synergy gives higher removal and good long-term stability | [40] |
| CAGH (straw-derived carbon aerogel with in situ loaded honeycomb/2D-filament g-C3N4H2O-N2-450-3h) | Gaseous toluene (1000 mg/m3 ≈ 250 ppm) | Visible light (435 nm) | 2 L quartz round-bottom flask or custom reactor | Line-surface binding mode enhances loading and exposes active sites; good cyclic stability | [41] |
| Bi2O3/Bi/TiO2 (sandwich structure with Bi embedded at heterojunction interface, 1 wt% Bi) | Gaseous toluene (300 ppm, 80% RH optimal) | UV light (4 × 4 W, 254 nm) | Continuous flow quartz tube reactor (10 mL/min) | Bi acts as electron-withdrawal mediator; sandwich structure prevents intermediate poisoning; sustained ROS generation gives excellent durability | [42] |
| 1D/2D Bi2WO6 (electrospun biomimetic eucalyptus-leaf structure with interpenetrating nanofibers and nanosheets, exposing {010} facets) | Gaseous acetaldehyde | Visible light (300 W Xe lamp, >420 nm) | Closed quartz reactor | 1D/2D network prevents nanosheet stacking; enhanced charge separation and abundant oxygen vacancies lead to full degradation and excellent stability | [43] |
| 0D/1D/2D Bi-BWO-250 (Bi0 nanosphere networks selectively grown on 1D/2D BWO heteromorphic junctions via H2/Ar reduction) | Gaseous acetaldehyde | Visible light (300 W Xe lamp, >420 nm) | Closed quartz reactor (evacuation system) | Synergistic effect of Bi0 network and oxygen vacancies enhances charge separation and extends light absorption (bandgap 2.21 eV) | [44] |
| CuBi2O4/CeO2−x (CC15, S-type heterojunction, rich oxygen vacancies) | Gaseous toluene (1800 ppm) | Full spectrum (300 W Xe lamp) | 100 mL square batch reactor with gas circulation (80 °C) | S-scheme heterojunction and oxygen vacancies enhance charge separation and ROS (•O2−, •OH) generation; strong interfacial interaction gives outstanding reusability | [45] |
| Bi2MoO6/WO3-3 (S-scheme heterojunction, WO3 nano-blocks anchored on Bi2MoO6 nanoflower spheres) | Gaseous formaldehyde (600 ppm) | Simulated sunlight (300 W Xe lamp) | Closed quartz reactor with fan circulation (25 °C, 40% RH) | S-scheme promotes charge separation and generates •O2− and •OH; effective for multiple VOCs; good humidity resistance and stability | [46] |
| NH2-MIL-125 (N100, 100% NH2-functionalized Ti-MOF) | Gaseous o-xylene (25 ppm for photocatalysis) | Visible light (Xe lamp, λ > 420 nm) | Continuous flow gas–solid dynamic system (40% RH) | NH2 groups act as adsorption sites (H bonding for o-xylene, Lewis acid–base for acetaldehyde); enhanced ROS generation due to easier photoexcitation and suppressed recombination | [47] |
| Fc-CHO/NU-2 & Fc-CHO/NU-3 (ferrocene carboxaldehyde-functionalized reo-NH2-UiO-66 via Schiff–base reaction) | Gaseous toluene (20 ppm) & acetaldehyde (200 ppm); also mixed VOCs | Visible light (Xe lamp, λ > 420 nm) | Fixed-bed flow reactor (N2 carrier gas, 40% RH) | Fc-CHO introduces Fe-OH and cyclopentadienyl rings as new adsorption sites; enhances LMCT, electron–hole separation, and ROS generation; π-π stacking promotes toluene ring-opening | [48] |
| IL-3DGr/NM(Ti) (amino-ionic liquid-bridged 3D-graphene/NH2-MIL-125 nanohybrids; 5 µmol IL) | Gaseous acetaldehyde (300 ppm) | Visible light (Xe lamp) | 350 mL quartz-lined glass jar (static air, 80 RH%) | IL bridging creates abundant coordinatively unsaturated sites and oxygen vacancies; activity increases with RH up to 80%; excellent stability | [49] |
| Zr10Ti1-U6N-300@TiO2 (bimetallic MOF derivative calcined at 300 °C, then loaded with TiO2 via hydrothermal method) | Gaseous toluene | UV–vis light | Dynamic flow reactor (360 min) | Z-scheme heterojunction between MOF derivative and TiO2 enhances charge separation; more oxygen vacancies and Lewis acid sites than references | [50] |
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Feng, X.-J.; Shi, X.; Zhang, H.-Y.; Huang, C.-H.; Yu, Q.-B. Research Progress on Novel Semiconductor Photocatalysts for Degrading VOCs. Catalysts 2026, 16, 356. https://doi.org/10.3390/catal16040356
Feng X-J, Shi X, Zhang H-Y, Huang C-H, Yu Q-B. Research Progress on Novel Semiconductor Photocatalysts for Degrading VOCs. Catalysts. 2026; 16(4):356. https://doi.org/10.3390/catal16040356
Chicago/Turabian StyleFeng, Xiu-Juan, Xin Shi, Hao-Yu Zhang, Chu-Hao Huang, and Qing-Bo Yu. 2026. "Research Progress on Novel Semiconductor Photocatalysts for Degrading VOCs" Catalysts 16, no. 4: 356. https://doi.org/10.3390/catal16040356
APA StyleFeng, X.-J., Shi, X., Zhang, H.-Y., Huang, C.-H., & Yu, Q.-B. (2026). Research Progress on Novel Semiconductor Photocatalysts for Degrading VOCs. Catalysts, 16(4), 356. https://doi.org/10.3390/catal16040356

