| 1 | Compare Specific Energy Consumption | Electricity used per cubic metre of treated water | Brackish-water RO: approximately 0.5–2.0 kWh/m³ Seawater RO: approximately 2.5–6.0 kWh/m³ | Request test data based on the actual feed-water salinity, temperature, recovery rate, and operating pressure. Confirm whether the quoted figure includes high-pressure pumps, pretreatment, controls, and energy-recovery equipment. |
| 2 | Check Water Recovery and Concentrate Volume | Percentage of feed water converted into permeate | Common industrial range: approximately 50–85% Higher recovery may require more advanced pretreatment | Calculate daily concentrate production before purchase. A system treating 100 m³/day at 75% recovery produces about 75 m³/day of permeate and 25 m³/day of concentrate. Verify scaling, fouling, and discharge constraints at the proposed recovery rate. |
| 3 | Evaluate Concentrate and Sludge Management | Waste-stream handling, disposal route, and compliance risk | Concentrate volume equals feed flow minus permeate flow; pretreatment may also generate chemical sludge or spent media | Confirm whether the site can use sewer discharge, permitted surface-water discharge, evaporation, deep-well injection, or off-site disposal. Obtain local approval requirements for salinity, pH, metals, cleaning chemicals, and sludge classification. |
| 4 | Review Pretreatment Requirements | Feed-water quality and protection of RO membranes | Typical controls include filtration, cartridge filtration, antiscalant dosing, pH adjustment, and disinfection management | Ask for design limits for turbidity, SDI, hardness, iron, manganese, oil, silica, chlorine, and biological activity. Free chlorine must generally be removed before polyamide membranes because it can damage the membrane material. |
| 5 | Estimate Total Operating Cost | Energy, membranes, chemicals, labor, cleaning, and waste disposal | Membrane replacement is often planned at roughly 3–7 years, depending on feed quality and maintenance; cleaning frequency varies from monthly to several times per year | Build a five-year cost model using local electricity prices, chemical consumption, labor rates, membrane replacement, laboratory testing, scheduled maintenance, and concentrate disposal. Avoid comparing systems using purchase price alone. |
| 6 | Verify Permeate Quality and Monitoring | TDS, conductivity, rejection, flow, pressure, and alarms | Salt rejection commonly starts around 95–99% for many industrial RO applications, depending on membrane type and feed conditions | Define guaranteed permeate limits for conductivity or TDS and specify how they will be tested. Require continuous monitoring of feed and permeate conductivity, pressure, flow, temperature, and operating hours, with automatic shutdown for critical faults. |
| 7 | Confirm Lifecycle Service and Spare Parts | Maintainability, local support, and parts availability | Critical consumables may include cartridge filters, seals, dosing components, cleaning chemicals, instruments, and replacement membranes | Check commissioning support, operator training, remote diagnostics, preventive-maintenance schedules, spare-parts lead times, warranty conditions, and documentation. Select standard electrical components suitable for the destination country's voltage, frequency, and certification requirements. |
| Planning note: The ranges above are general industrial reference values, not guaranteed performance figures. Final energy use, recovery, permeate quality, waste volume, and operating cost must be confirmed through a site-specific water analysis, pilot testing where necessary, and local discharge regulations. |