Dissolved salts removed by membranes — for boiler feed, process water, drinking water and reuse.
Reverse osmosis pushes water through a semi-permeable membrane at pressure, leaving 95–99 % of dissolved salts, most organics and essentially all micro-organisms behind in a concentrate stream. It is the standard way to bring TDS down — from a few hundred mg/L in borewell water, to several thousand in brackish or effluent-reuse water, to 35,000 mg/L in seawater.
An RO plant is only as good as its pretreatment. Suspended solids, colloids, hardness, iron, silica, chlorine and biology all foul or damage membranes; recovery and antiscalant chemistry decide whether the plant runs at design output for years or fouls in months. We design the complete train — not just the skid.
TDS up to ~10,000 mg/L; industrial process, drinking, boiler feed.
Treated ETP/STP outlet to process or cooling water; fouling-resistant design.
Two stages for pharmaceutical purified water or high-purity boiler feed.
Energy recovery, high-rejection membranes, duplex/super-duplex materials.
Factory-built, plug-and-play for remote or temporary sites.
Feed analysis and projection (membrane software) → pretreatment and recovery selection → skid design, P&ID, instrumentation → supply, erection, commissioning → membrane performance monitoring under O&M.
Brackish-water RO typically recovers 70–80 % of the feed as permeate; two-stage or high-recovery designs reach 85–95 % where scaling is controlled. Seawater RO recovers 35–45 %.
At minimum multimedia or ultrafiltration, cartridge filtration, chlorine removal and antiscalant dosing. Hardness, iron, silica and organics decide whether softening, oxidation or activated carbon is also required.
With proper pre-treatment and cleaning, 3–5 years for industrial plants; poorly pre-treated plants can lose membranes in months. We design the pre-treatment to protect the membranes, not the other way round.
Reject can be used for floor washing, dust suppression or blended into non-critical uses; where discharge is not permitted it goes to an evaporator as part of a ZLD scheme.
Share your inlet analysis, capacity and location — we reply with a preliminary scheme and budget range within one working day.