| Compact light-commercial RO | 250–1,000 gallons per day (GPD) | Municipal or low-to-moderate salinity brackish water | About 50–70% | Sediment filtration; carbon treatment when chlorine is present | Small cafés, clinics, and low-volume food-service operations | A compact arrangement suited to modest demand and limited installation space. |
| Restaurant and hospitality RO | 500–5,000 GPD | Municipal water or suitably pretreated well water | About 50–75% | Sediment filtration, dechlorination where needed, and scale control based on water analysis | Restaurants, hotels, beverage stations, and commercial kitchens | Provides treated water for multiple points of use; storage tanks can help meet short demand peaks. |
| Office and campus RO | 2,000–20,000 GPD | Municipal or brackish groundwater | About 50–75% | Particle filtration, chlorine removal if required, and antiscalant or softening when indicated | Large offices, schools, and institutional drinking-water systems | Centralized treatment can supply several users or downstream distribution points. |
| Boiler-makeup RO | 1,000–50,000 GPD | Municipal or well water, selected for the boiler’s feed-water requirements | About 50–75% | Filtration and scale-control pretreatment; softening may be used depending on feed chemistry | Commercial and industrial boiler makeup | Reduces dissolved solids entering the makeup-water treatment train; additional polishing may be needed for the boiler. |
| Food and beverage process-water RO | 2,000–50,000 GPD | Municipal or suitably treated groundwater | About 50–75% | Sanitary-compatible filtration and dechlorination as needed; pretreatment selected from water analysis | Food processing, beverage production, and ingredient-water preparation | Can provide a consistent treated-water supply; hygienic design and sanitation procedures matter. |
| Brackish-water RO for higher dissolved-solids feeds | 1,000–50,000 GPD | Brackish groundwater or other saline inland sources | Often about 50–75%; feed chemistry can require lower recovery | Cartridge or media filtration, scale control, and iron or manganese removal when present | Facilities using wells with elevated dissolved salts | Membrane selection and operating pressure are matched to feed salinity and target permeate quality. |
| High-recovery brackish-water RO | 1,000–50,000 GPD | Relatively consistent brackish feed suitable for staged concentration | Approximately 65–80% in suitable designs; not appropriate for every feed | Thorough filtration and chemistry-based scale control; feed-water testing is essential | Sites seeking to reduce reject-water volume where feed quality permits | Staging or specialized concentrate management can raise recovery, but scaling risk and concentrate disposal must be assessed. |
| Single-pass seawater RO | 1,000–50,000 GPD | Seawater | Generally about 35–50% | Fine filtration, often including ultrafiltration or equivalent pretreatment, plus seawater-compatible materials | Coastal commercial facilities and marine-related operations | Uses higher operating pressure than brackish-water RO because seawater has substantially greater salinity. |
| Containerized or modular seawater RO | 10,000–250,000 GPD | Seawater or high-salinity source water | Generally about 35–50% | Intake screening and fine filtration; pretreatment depends on turbidity and biological loading | Remote sites, coastal facilities, and temporary or modular water-supply projects | Integrates major treatment components in a modular layout; intake quality and reject disposal remain site-specific considerations. |
| Two-pass RO or RO with EDI polishing | 1,000–100,000 GPD, depending on configuration | First-pass RO permeate or other suitable pretreated feed | Overall recovery varies; often roughly 45–70% for two-pass arrangements | First-pass RO pretreatment; additional protection and monitoring for the second pass or EDI stage | Laboratories, pharmaceutical support systems, and applications requiring higher-purity water | A second RO pass or electrodeionization (EDI) can further reduce ionic content; final quality depends on the complete treatment train. |