| Advantages | Dares |
Oxidants | ||
Cl2 | CI− is among the most abundant anions in most waters; lower standard potentials than most electrochemically generated oxidants; longer lifetimes allow for disinfection residual; can combine with ammonia to form chloramines with lower DBPs and more stable residual. | CI− must be present in sufficient concentration or externally supplied; many oxidized CI species are toxic ( , , etc.); current efficiency depends on CI− concentration, limiting performance in low salinity waters; can generate chlorinated DBPs (e.g., trihalomethanes and haloacetic acids). |
•OH | Strongest disinfectant among common electrochemically generated oxidants; can be generated without specific precursor ions (e.g., Cl−); can also oxidize total organic carbon (TOC) and many micropollutants; capable of treating Cryptosporidium at practical doses. | Highest standard potential of common electrochemically generated oxidants; radical species have very low lifetimes in solution; can generate and brominated compounds in Br− containing waters. |
Treatment context | ||
Drinking water | Low organic carbon levels reduce scavenging and necessary dose, depending on placement in treatment train; does not require onsite hazardous chemical storage; lower overall dose required compared to wastewater. | May require CI− addition if CI oxidant species are desired; most oxidants produced electrochemically have shorter lifetime, making residual generation difficult. |
Centralized wastewater | CI− concentration is usually sufficient to generate CI oxidant; high levels can scavenge more oxidized CI species ( , , etc.) and produce chloramine; dose can be dynamically adjusted during severe events. | High carbonaceous chemical oxygen demand (cCOD) levels introduce competition for oxidant; electrochemical systems typically scale linearly for cost and energy demand. |
Distributed wastewater | Electrochemical systems can be easily scaled down for portable units; a single unit can be used to electrochemically generate oxidants for simultaneous treatment of cCOD, , and pathogens. | Higher energy inputs are required for treatment of multiple target species; electrochemical systems typically have high capital cost compared to other methods. |