Clearflow RO-SW 2000
Full seawater desalination hall — six parallel banks with isobaric energy recovery.
- 200 m³/hPermeate
- 99.78 %Rejection
- 45 %Recovery
- 2.58 kWh/m³Specific energy
Seawater RO train with isobaric energy recovery for coastal potable and process supply.
A complete seawater train on one skid: fifteen vessels, an API 610 BB2 pump and a pressure exchanger that hands the brine energy straight back to the feed.
The Clearflow RO-SW 450 is a standard Clearflow configuration rated at 45 m³/h of permeate at 45 % system recovery, which is 1,080 m³ over a continuous day. The published envelope assumes 25 °C, a clean membrane and the design feed analysis; every project is re-projected against the water you actually have before a price is issued.
The array is arranged as single stage, 15 vessels in parallel, 6 elements per vessel. Element type is SW 8040 high-rejection, 37.2 m² each, running on high-rejection seawater polyamide. Design flux is held at 13.4 LMH so the concentrate velocity through the last element stays inside the manufacturer envelope at design recovery — the single most reliable predictor of how long the membranes will last.
| Parameter | Design value | Note |
|---|---|---|
| Feed pressure | 58.0 bar | At design feed TDS and 25 °C |
| Trans-membrane differential | 2.40 bar | Clean; change-out trigger at twice this value |
| Feed temperature | 8–40 °C | Output falls roughly 3 % per °C below 25 °C |
| Continuous pH | 3.0–10.0 | Wider band tolerated during cleaning |
| Free chlorine | Max 0.10 mg/L | Continuous exposure limit at the membrane face |
| Concentrate flow | 55.0 m³/h | At design recovery |
Three-stage CIP with heated tank, 4,000 L. Control is by Industrial PLC with normalised performance trending and remote access. The wetted specification is Super duplex 2507 high-pressure side, duplex 2205 manifolds. Pressurisation is by API 610 BB2 duplex barrel pump, 58 bar discharge; PX isobaric pressure exchanger, 95 % transfer efficiency.
| Permeate capacity | 45 m³/h |
|---|---|
| Daily output at 24 h | 1,080 m³/d |
| System recovery | 45 % |
| Design feed flow | 100 m³/h |
| Concentrate flow | 55 m³/h |
| Nominal rejection | 99.75 % |
|---|---|
| Typical permeate TDS | 149.4 mg/L |
| Design flux | 13.4 LMH |
| Feed pressure | 58 bar |
| Trans-membrane ΔP | 2.40 bar |
| Specific energy | 2.62 kWh/m³ |
| Max feed TDS | 45,000 mg/L |
|---|---|
| Min design feed TDS | 18,000 mg/L |
| Max feed SDI15 | 4.0 |
| Max feed turbidity | 0.20 NTU |
| Min feed temperature | 8 °C |
| Max feed temperature | 40 °C |
| Min continuous pH | 3.0 |
| Max continuous pH | 10.0 |
| Max free chlorine | 0.10 mg/L |
| Membrane elements | 90 pcs |
|---|---|
| Pressure vessels | 15 pcs |
| Elements per vessel | 6 pcs |
| Stage 1 vessels | 15 pcs |
| Stage 2 vessels | 0 pcs |
| Array configuration | Single stage, 15 vessels in parallel, 6 elements per vessel |
| Element type | SW 8040 high-rejection, 37.2 m² each |
| Membrane chemistry | High-rejection seawater polyamide |
| Active membrane area | 3,348 m² |
| Pressure pump | API 610 BB2 duplex barrel pump, 58 bar discharge |
|---|---|
| Energy recovery | PX isobaric pressure exchanger, 95 % transfer efficiency |
| Wetted materials | Super duplex 2507 high-pressure side, duplex 2205 manifolds |
| Control system | Industrial PLC with normalised performance trending and remote access |
| Cleaning regime | Three-stage CIP with heated tank, 4,000 L |
| Skid footprint L×W×H | 9.8 × 2.4 × 3.0 m |
| Dry shipping weight | 11,800 kg |
| Installed motor load | 160 kW |
| Indicative lead time | 18–22 weeks ex works |
Send us the feed analysis and duty flow and we will re-project this array against your water.
Full seawater desalination hall — six parallel banks with isobaric energy recovery.
Send us the duty flow, the feed water analysis and the permeate specification you have to hit. Our process desk replies within one working day.