Engineering Case: 5000 T/D Pretreatment + 4000 T/D RO — Singapore (Mine-Water Reuse)

Scenario: Reuse of mine/process water inside a factory area. System capacity combines a 5000 T/D pretreatment line feeding a 4000 T/D single-stage RO, with automated operation and stable permeate quality for utilities and production.

Country / SiteSingapore / industrial mining-water reuse inside plant
Total CapacityPretreatment 5000 T/D (≈208 m³/h) → RO 4000 T/D (≈167 m³/h)
Influent RisksSuspended solids, fines, turbidity swings; dissolved metals; occasional hydrocarbons; scaling species (Ca, Ba, Sr, silica).
Process Train Equalization → coagulation/flocculation → lamella clarifier (or DAF per influent) → multimedia filtration → activated carbon (organics & de-chlorination) → optional UF (SDI control) → 5 µm cartridge → RO (8040 brackish) → permeate tank & distribution.
MaterialsHP RO piping SS316; pretreatment vessels carbon-steel lined / FRP; skids SS304; chemical-resistant elastomers.
ContrôlesPLC + HMI; trend logging for turbidity/SDI/ΔP/cond; interlocks to EQ tanks; auto permeate flush & standby modes.

Design Basis & Targets

  • Recovery: RO set around 70–75% (balancing silica/metals scaling indices and flux).
  • Permeate quality: typically ≤ 30–50 µS/cm for utilities; polishing options available if ultra-low conductivity is required.
  • SDI control: ≤ 3 at RO inlet; UF module enabled when seasonal fines increase.
  • Metal risk management: pH conditioning and coagulant selection validated via jar tests.
  • CIP readiness: dedicated CIP tank/pumps, validated acid/alkali recipes per membrane OEM limits.

Process Highlights

  • Equalization & clarification buffer shock loads; lamella plates or DAF chosen by oil/fines ratio.
  • Dual-media filters + ACF stabilize turbidity and remove oxidants/organics ahead of RO.
  • RO arrays with VFD HP pumps, interstage sampling, and programmable flush to protect membranes.
  • Chemical program: antiscalant; optional sodium metabisulfite or carbon for de-chlorination; non-oxidizing biocide as needed.
  • Brine handling: segregated blowdown to plant utilities for further treatment/disposal per local regulation.

Commissioning & Handover

  • FAT → SAT → performance run with water balance and quality mapping (influent/RO feed/permeate/brine).
  • Training: SDI testing, log-sheet KPIs (flow, pressure, ΔP, conductivity), CIP trigger thresholds.
  • Deliverables: P&ID, layout, I/O list, SOPs, PM plan, membrane cleaning record templates.
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