Suspended |
Baffled reactor using Degussa P25-TiO2 NPs |
Acid orange 52 (50 mg/L) |
Complete mineralization after 30 h at a flow rate of 14.4 L/h |
[41] |
Submerged membrane photocatalysis reactor (SMPR) using UV/TiO2
|
Rhodamine B |
95% removal was observed at a catalyst loading of 0.1 g/L under 3 ultraviolet (UV) c lamps at pH 8 |
[42] |
Slurry photoreactor having mesoporous TiO2 NPs |
Dichlorophenol-indophenol (DCPIP) dye (1 to 4 × 10−4 mol/L) |
96.4% DCPIP degradation occurred within 3 min at 1 × 10−4 mol/L concentration and pH 3 |
[43] |
Packed bed photoreactor |
Phenazopyridine (10, 20, 30, 40 mg/L) |
90% decrease in TOC was observed after 150 min |
[44] |
Photocatalytic drum reactor having TiO2 NPs |
MB (10 μM) and 4-Chlorophenol (100 μM) |
93% MB degradation after 15 min and 94% 4-CP removal after 90 min |
[45] |
Rotating drum reactor having Degussa P25-TiO2
|
MB |
98% of MB removal was observed at 30 g/L TiO2 after 60 min |
[46] |
Immobilized |
Thin-film fixed bed reactor having TiO2 NPs |
Carmoisine dye (10 mg/L) |
97% removal was observed at pH 2 after 45 min at a flow rate of 0.25 L min−1
|
[47] |
Baffled reactor immobilized with TiO2 NPs |
Acid orange 52 (AO52) (50 mg L−1) |
After 4 h, dye converted into benzene annular compound, intermediates gradually decreased after 10 h and complete mineralization into CO2 and H2O in 30 h |
[41] |
Rotating disc photoreactor, TiO2 (P25) immobilized on High Density Polyethylene (HDPE) plate |
p-nitrophenol (15 mg L−1) |
83% removal was observed at pH 5 after 118 min at 800 mL volume |
[48] |
Rotating aluminum drum with TiO2-coated corrugated aluminum drum |
Tetracycline (0.5, 1, 5, 10, 30, 50, 60, and 80 ppm) |
93% Tetracycline was observed after 20 min |
[49] |
Spiral photoreactor system sintered with TiO2 thin film |
4-tert-octylphenol (4-t-OP) (2, 5, 8 and 10 mg L−1) |
90% 4-t-OP degradation was observed at 10 mg/L concentration with single layer TiO2 film (13.6% TiO2 precursor) |
[50] |