Review Article
Recent Overview of Solar Photocatalysis and Solar Photo-Fenton Processes for Wastewater Treatment
Table 5
Immobilized TiO2 solar photocatalysis.
| Contaminant (concentration interval) | Experimental conditions | Reactor | Best degradation conditions | Reference | Name | Initial concentration | Method of synthesis | Catalyst (pH) | Initial concentration | Type of reactor | Total volume | Percentage | Time |
| Atrazine | 20 mg L−1 | Sol-gel method using titanium butoxide | 180 spheres of TiO2-coated glass sustained by a nylon mesh (3.0) | 0.3 g L−1 | An open, undivided and cylindrical tank reactor | 200 mL | Reduction of 30% of initial concentration | 300 min | [202] | Methylene blue | 50 mg L−1 | Hydrothermal method | TiO2 Degussa P25 supported on black volcanic ashes TVA (no pH adjustment) | 3 g L−1 TVA | Stirred photoreactors with parabolic sunlight irradiation concentrators | 50 mL | 95% degradation of wastewater pollutant | 120 min | [210] | Salicylic acid | 165 mg L−1 | Sol-gel method using titanium butoxide | TiO2 coating onto borosilicate glass spheres of 5 mm diameter (3.0) | 0.25 g TiO2 L−1 | A polycarbonate box with a mirror at the bottom and tilted 41° | 3.0 L | Reduction of 14% of initial concentration | 360 min | [194] | Acetaminophen, thiabendazole, acetamiprid, and imazalil | 100 μg L−1 each | Sol-gel technique using titanium isopropoxide | Glass spheres (6 mm φ) were dip-coated with the TiO2 sol (6.2–8.4) | 0.6 mg of TiO2 on the surface of each glass bead | CPC | 8 L | Reduction of 100% of initial concentration | 240 min | [122] |
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