Factor | Initial concentration (mg/L) | Degradation rate and time | Advantages | Disadvantages | References |
---|---|---|---|---|---|
Photochemical | |||||
TiO2-NPs | 10 | 100% in 2 h | High degradation rate | Low initial concentration | [31] |
Boric/Cerous co-doped TiO2 | 0.2 | 83% in 0.5 h | Short time | Low initial concentration | [32] |
Ag/TiO2-NTs | 100 | 72% in 20 min | Short time and high initial concentration | Low degradation rate | [33] |
Sonochemical | |||||
Hydrodynamic cavitation | 50 | 85% in 1 h | Short time | Difficult to apply | [34] |
Electrochemical | |||||
BDD electrode | 50 | 100% in 3 h | High degradation rate | High cost | [35] |
Oxidation | |||||
H2O2 | 0.6 | 100% in 100 min | High degradation rate | Low initial concentration | [36] |
O3 | 0.16 | 98% in 1 h | High degradation rate | Low initial concentration | [37] |
Biological | |||||
Pseudomonas sp. PFD9 | 10 | 70% in 24 h | Low cost and easy to operate | Low initial concentration and degradation rate | [30] |
Pseudomonas sp. PFD13 | 10 | 32% in 24 h | Low cost and easy to operate | Low initial concentration and degradation rate | |
Exiguobacterium acetylicum MA4 | 5 | 95% in 24 h | High degradation rate and low cost | Low initial concentration | [27] |
Bacillus megaterium SSF1 | 5 | 93% in 24 h | High degradation rate and low cost | Low initial concentration | |
Strain DSPM95 | 20 | 95% in 31 days | High degradation rate and low cost | Long time | [38] |
Datronia concentrica | 20 | 99% in 31 days | High degradation rate and low cost | Long time | |
Cellulase | 10 | 72% in 7 h | Easy to operate and obtain | Low initial concentration and degradation rate | [28] |
Activated sludge | 1 | 97% in 18 days | Easy to obtain and high degradation rate | Low initial concentration and anaerobic | [29] |