Desalination Plant Chemical Program Design
6 min read·
desalinationROseawaterpretreatment
Chemical Program Overview
| Treatment Stage | Chemical | Purpose | Typical Dose |
|---|---|---|---|
| Intake | NaOCl | Biofouling prevention | 1–3 ppm Cl₂ (shock) |
| Pre-chlorination | Sodium bisulfite | Dechlorination before RO | 3 ppm (stoichiometric) |
| Coagulation | FeCl₃ or membrane flocculant | SDI reduction | 1–5 ppm |
| pH adjustment | H₂SO₄ | Lower pH for CaCO₃ control | To pH 6.5–7.0 |
| Antiscalant | RO antiscalant | Scale prevention | 2–5 ppm |
| CIP cleaning | Alkaline + acid cleaners | Restore membrane performance | 2–4% solution |
| Post-treatment | Ca(OH)₂ + CO₂ | Remineralization | To LSI ~0 |
| Final disinfection | NaOCl | Residual disinfection | 0.2–0.5 ppm Cl₂ |
Pretreatment Design
Goal: SDI < 3, turbidity < 0.5 NTU, zero chlorine.
Options (from basic to advanced):
- Conventional: Coagulation + sand filter + cartridge filter
- UF/MF: Direct membrane pretreatment (preferred for new plants)
- DAF + UF: For high-algae source water
Critical: Remove ALL free chlorine before RO membranes — polyamide membranes are destroyed by oxidants.
Antiscalant Selection for Desalination
Seawater RO: General purpose antiscalant typically sufficient (recovery 35–45%) Brackish water RO: May need high-hardness grade at high recovery (75–90%)
Dose calculation: Based on concentrate composition, not feedwater.
CIP Schedule
| Indicator | Action |
|---|---|
| Normalized permeate flow −10% | Clean (alkaline first, then acid) |
| ΔP +15% | Clean (check for biofilm) |
| Salt passage +50% | Clean (check for scaling) |
| Every 3–6 months | Preventive CIP even if no decline |
Post-Treatment
RO permeate is aggressive (low pH, low alkalinity, low hardness). Remineralization required:
- Lime + CO₂: Ca(OH)₂ saturator + CO₂ injection → target LSI ≈ 0, pH 7.5–8.5
- Limestone contactor: Permeate through calcite bed — simpler but slower
- Add NaOCl for final disinfection residual
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