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Hollow Fiber Ultrafiltration Membrane Cooling Water System Water Supply Process

by endalton 19 May 2025


Process Flow of Hollow Fiber Ultrafiltration Membrane Cooling Water System Water Supply

  1. Raw Water Pretreatment Stage
    • Mechanical Filtration
      • Multimedia Filter: Removes suspended solids (SS), silt, rust, etc. The filter media are quartz sand and anthracite coal, with a filtration accuracy of ≤50μm.
      • Self-Cleaning Filter (Optional): Fully automatic backwashing to protect the ultrafiltration membrane from large particle impacts.
    • Water Quality Adjustment
      • Disinfection and Algae Control: Add sodium hypochlorite (1-3mg/L) or non-oxidizing biocides to inhibit microbial growth.
      • pH Adjustment: If the raw water is acidic (e.g., pH<7), add NaOH to adjust to neutral (pH 6.5-7.5) to reduce membrane fouling.
  2. Ultrafiltration Membrane Treatment Stage
    • Membrane Module Selection
      • Material: Hollow fiber membranes made of polyvinylidene fluoride (PVDF) or polyethersulfone (PES), which are resistant to oxidation and fouling.
      • Pore Size: 0.01-0.1μm, capable of retaining bacteria (99.99%), colloids, and large molecular organic substances (such as humic acid).
      • Membrane Flux: Design flux of 50-100LMH (liters/square meter·hour), with a conservative value chosen based on water quality.
    • Operation Mode
      • Full Flow Filtration/ Cross Flow Filtration: For low-pollution water quality, full flow filtration is used (recovery rate ≥90%); for high-pollution water quality, cross flow filtration is used (recovery rate 70-85%).
      • Backwashing: Every 30-60 minutes, combined air and water backwashing (0.1-0.3MPa, lasting 30 seconds) is performed to restore membrane flux.
    • Key Parameters
      • Operating Pressure: 0.1-0.3MPa
      • Inlet Water Temperature: 5-40℃ (to avoid membrane aging due to high temperature)
      • Transmembrane Pressure Difference (TMP): ≤0.15MPa (chemical cleaning is triggered when exceeded)
  3. Post-Treatment and Recirculation
    • Scale and Corrosion Inhibition Treatment
      • Scale Inhibitor Addition: Add scale inhibitors (such as polyacrylic acid) to the ultrafiltration product water to prevent scaling in the recirculating cooling water system (CaCO₃, CaSO₄).
      • Corrosion Inhibitor Addition: Add corrosion inhibitors (such as molybdates) to protect the metal surfaces of pipes and heat exchangers.
    • Recirculating Water System
      • The ultrafiltration product water enters the cooling tower or heat exchanger for recirculation. The concentrate (backwash drainage) is discharged to the wastewater treatment system or reused.
  4. Maintenance and Management
    • Chemical Cleaning
      • Frequency: Every 3-6 months or when TMP increases by 20%.
      • Cleaning Agents: 0.1% NaOH + 0.05% NaClO (for removing organic matter and biological contamination); 0.2% citric acid (for removing inorganic scale).
    • Membrane Lifespan: Under normal maintenance, the lifespan is 3-5 years, with a flux attenuation rate of ≤10%/year.

Brief Scheme Design

Core Equipment Configuration
  • Pretreatment Unit: Multimedia filter, dosing equipment (biocides, pH adjusters)
  • Ultrafiltration System:
    • PVDF hollow fiber ultrafiltration membrane modules (e.g., SFP-2660 type)
    • Backwashing pump, compressed air system, PLC automatic control system
  • Post-Treatment Unit: Scale inhibitor dosing pump, corrosion inhibitor dosing equipment
  • Recirculation System: Cooling tower, heat exchanger, recirculation pump
Expected Water Quality Indicators
Item Inlet Water Quality (Typical Value) Ultrafiltration Product Water Quality
Turbidity (NTU) ≤20 ≤0.2
SDI15 (Pollution Index) ≤5 ≤3 (meets the requirements for reverse osmosis feed water)
Total Bacteria Count (CFU/mL) ≤10⁴ ≤10
TOC (mg/L) ≤5 ≤1
Advantages and Precautions
Advantages
  • High-Efficiency Retention: Thoroughly removes suspended solids, colloids, and microorganisms, reducing the risk of scaling and corrosion in the cooling water system.
  • Low Energy Consumption: Low operating pressure (0.1-0.3MPa), with lower operating costs compared to reverse osmosis.
  • Automation: PLC control can achieve automatic backwashing, dosing, and fault alarms.
Precautions
  • Water Quality Monitoring: Real-time monitoring of SDI, TOC, and residual chlorine to avoid damage to membrane materials from excessive oxidants.
  • Concentrate Water Treatment: Backwash drainage contains high concentrations of pollutants and should be included in the plant's wastewater system for treatment.
  • Freeze Protection: In cold regions, insulation of membrane modules and pipes is required to prevent freezing and cracking.
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