Table 4.
Method | Removal/inactivation log |
Merits | Limitations |
---|---|---|---|
Membrane filtration | 0.5–5.9 | Low energy cost, the potential for mobile treatment unit, does not require chemicals | Removal efficiency is unstable, a potential health risk for humans |
Ultraviolet irradiation | 0.09–5 | No DBPs formation, less susceptible to pH and temperature, non-corrosive, ease of installation and operation, short contact time | Relatively high energy consumption, inefficient in turbid water |
Chlorination | 1- > 5 | Simple to handle, cost-effective, residual in distribution | DBPs production, residual toxicity |
Monochloramination | 0.5–4 | Stable residual, less odor, and taste issues | Weak disinfectant, less virucidal, long contact time |
Chlorine dioxide | 0.25–6 | More effective than chlorine at higher pH, lowers DBPs formation | DBPs formation, organoleptic abnormalities |
Ozonation | 0.6–7.7 | Effective disinfectant, short contact time, possible combination with various catalysts | DBPs formation, high operation and maintenance cost, non-stable and poor solubility, effectiveness is affected by water turbidity |
Photocatalytic disinfection | 1–8 | Low cost of operation, possible reuse of catalysts, favorable catalytic performance | Accidental leaching of hazardous metals into treated water |
Cavitation | <4 | No DBPs formation, possible for incorporation into a continuous flow process | Energy-intensive and high operating cost, still at the developmental stage |
Electrochemical disinfection | 3.4–5 | Easy to control, environment friendly | Possibility of DBPs formation, low selectivity, the high operating cost associated with electricity consumption |