| Reverse Osmosis (RO) | Pressure-driven membrane separation for dissolved salts, ions, many metals, nitrate, fluoride, and numerous dissolved contaminants. | Typically removes about 95–99% of total dissolved solids and many dissolved ionic contaminants when correctly designed and operated. Removal varies by contaminant, membrane, pH, temperature, and feedwater quality. | Approximately 0.3–1.5 kWh/m³ for many brackish-water systems; seawater systems commonly require about 3–6 kWh/m³ because of higher operating pressure. | 50–85% for many brackish-water and municipal designs. Seawater systems often operate at lower recovery, commonly around 35–50%. | Best option when low salinity, low conductivity, or broad dissolved-contaminant reduction is required. | Produces a concentrate stream, requires pretreatment, operates under pressure, and may be affected by scaling, fouling, and membrane degradation. |
| Ultrafiltration (UF) | Low-pressure membrane filtration for suspended solids, colloids, turbidity, bacteria, and protozoan cysts. | Can provide approximately 4–6 log removal of bacteria and protozoa with an intact, properly operated membrane. It generally provides limited and unreliable removal of dissolved salts and many small viruses. | Approximately 0.05–0.30 kWh/m³, depending on flux, transmembrane pressure, backwashing, feedwater quality, and system scale. | Often about 90–99%; lower values may occur when frequent backwashing or chemically enhanced cleaning is required. | Excellent turbidity and particulate control with lower pressure and energy requirements than RO. | Does not significantly reduce salinity, conductivity, hardness, or most dissolved chemicals; membrane integrity must be monitored. |
| Ultraviolet (UV) | Physical disinfection using ultraviolet light to damage the DNA or RNA of microorganisms. | Validated systems can achieve approximately 3–6 log inactivation of many bacteria, viruses, and protozoa at the specified UV dose. It does not remove dissolved chemicals, salts, turbidity, or particles. | Approximately 0.01–0.10 kWh/m³ for many drinking-water and process-water systems; power depends strongly on UV dose, flow, lamp efficiency, and water clarity. | Approximately 99–100% hydraulic recovery because there is normally no reject stream. | Rapid, chemical-free microbial control with no change to taste, salinity, or mineral content. | Requires low turbidity and good UV transmittance; provides no residual protection after treatment and requires lamp, sensor, and sleeve maintenance. |
| Granular Activated Carbon (GAC) | Adsorption of chlorine, taste and odor compounds, and selected organic contaminants. | Can remove more than 90% of free chlorine under suitable contact conditions. Organic-contaminant removal is highly variable and depends on carbon type, empty-bed contact time, concentration, temperature, and competing compounds. | No significant reaction energy; pumping commonly adds approximately 0.01–0.05 kWh/m³, excluding backwash and regeneration requirements. | Typically about 98–100% during normal flow; backwashing or carbon replacement creates a separate wastewater or solid-waste stream. | Effective pretreatment for chlorine and many taste-and-odor problems; can protect downstream membranes from oxidants. | Does not remove salts and is not a reliable stand-alone disinfection barrier. Exhausted carbon can release previously adsorbed contaminants if not replaced or regenerated on schedule. |