Review Article
Recent Overview of Solar Photocatalysis and Solar Photo-Fenton Processes for Wastewater Treatment
Table 6
Solar photocatalysis using nitrogen-doped TiO2, carbon-doped TiO2, polypyrrole TiO2 nanocomposites, and a mix of TiO2 with persulfate ions.
| Contaminant (concentration interval) | Experimental conditions | Reactor | Best degradation conditions | Reference | Name | Initial concentration | Catalyst (pH) | Initial concentration | Type of reactor | Total volume | Percentage | Time |
| Cefazolin | Concentration of 1.0 × 10−2 mol L−1 | N-doped TiO2 (6.4) | 2.0 g L−1 | Batch-type photoreactor | 600 mL | 80% of cefazolin removed | 30 min | [211] | Azo dye orange G | 25 mg L−1 | Nitrogen-doped TiO2 (2.0) | 1.0 g L−1 | Glass beaker | 1000 mL | Efficiency of degradation greater than 95% | 40 min | [212] | Methylene blue | 20 mg L−1 | Carbon-doped TiO2 nanoparticles (neutral pH) | 1.0 g L−1 | Batch-type photoreactor | 200 mL of 10 mg/L methylene blue | Greater than 0.1 Ct/Co | 60 min | [175] | Acid orange 7 in the concentration | 0.2 mM L−1 | Combination of TiO2 with potassium persulphate (3.0) | TiO2 (200 mg L−1) and 10 mM L−1of potassium persulphate | Photochemical reactor with recirculation | 300 mL | 90% of color removal COD removal depended on the persulfate ion concentration | 120 min | [13] | Methyl orange | 10 mg L−1 | Polypyrrole-TiO2 nanocomposites (no pH adjustment) | 0.45 g L−1 polypyrrole-TiO2 nanocomposites suspended | Glass beaker | 450 mL | ~90% initial concentration removal | 160 min | [213] | 4-Chlorophenol | 20 mg L−1 | Titania Degussa P-25 and activated carbon (no pH adjustment) | 0.2 g L−1 | Two CPC modules in connected in series | 247 L | ~100% initial concentration removal | At 2000 min W m−2 | [176] |
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