
Product Specification
Specification Size | Model | Unit | AD-UF3-HF51 | AD-UF3-HF77 | |
Average Membrane Pore Size | μm | 0.03 | 0.03 | ||
Membrane Area | m² | 51 | 77 | ||
Membrane Fiber Inner/Outer Diameter | mm | 0.7/1.3 | 0.7/1.3 | ||
Effective Length of Membrane Fiber | mm | 1380 | 1880 | ||
Installation Size and Method | - | Feed Water, Product Water, Concentrated Water Port DN50 Copy Lin | |||
Side Feed Water | Component dimensions (φ×H) | mm | φ225×1860 | φ225×2360 | |
Inlet Form | - | PT3/8" Conical Pipe Internal Thread | |||
Bottom Feed Water | Component dimensions (φ×H) | mm | φ225×1900 | φ225×2400 | |
Inlet Port Form | - | Component Inlet Pipe Connection with Bell Joint | |||
Weight | Empty Weight (including Quantitative Protective Liquid) | kg | 45 | 60 | |
Full Water Weight | kg | 80 | 100 | ||
Material | Membrane Fiber Material | PVDF | |||
Potting Adhesive | - | Epoxy Resin | |||
Membrane Tube Material | - | UPVC | |||
Maximum Inlet Turbidity | NTU | 300 | |||
Maximum Inlet Pressure | MPa | 0.30 | |||
Operating Conditions | Maximum Operating Temperature | ℃ | 40 | ||
Tolerable pH Range | 2~12 | ||||
Operating Mode | - | Crossflow or Dead-end Filtration |
[Note]: Other specifications of membrane products can be customized according to user needs.
Operating Conditions
Operating Parameters Backwash Parameters Maintenance Cleaning (MC) In-situ Recovery Cleaning (CIP) | Common Membrane Flux Range | HF:40~120L/(m² ·h) | |
Transmembrane Pressure Range | 30~150kPa | ||
Maximum Transmembrane Pressure During Filtration | 0.2MPa | ||
Maximum Inlet Pressure | 0.3MPa | ||
Maximum Inlet Turbidity | 300NTU | ||
Crossflow Filtration Backflow Rate | 10%~30% | ||
Maximum Particle Size | ≤300μm | ||
Total Suspended Solids | ≤100mg/L | ||
Working Temperature | 1-40℃ | ||
Backwash Method | Air-Water Backwash | ||
Design Backwash Frequency | 24~48 times/day | ||
Scrubbing Air Pressure During Backwash | ≤150kPa | ||
Backwash Flux | 0.5~1.5 times the product water flux | ||
Backwash Gas Flow Rate | 8~12Nm³/h (per unit) | ||
Backwash Gas Source | Oil-free Compressed Air | ||
Duration | 30~60s per cycle | ||
Method 1 (Low Concentration In-situ Cleaning L-CIP) | Cleaning Method | Low Concentration Citric Acid Solution or Sodium Hypochlorite Solution Internal and External Circulation Washing | |
Maintenance Cleaning Occupied Time | 50min (including washing time) | ||
Citric Acid Frequency | 1 time / 1 ~ 3 days / set | ||
Sodium Hypochlorite Frequency | 1 time / 1~3 days / set | ||
Washing Flow Rate | 1~2m³ per membrane component | ||
Maintenance Cleaning Chemical Concentration | 0.5%~1% Citric Acid 300~500ppm Sodium Hypochlorite | ||
Method 2 (Chemical Learn to strengthen backwashing CEB) | Cleaning Method | Add chemical agents to strengthen backwashing during water backwashing | |
Maintenance Cleaning Occupied Time | 15min | ||
Citric Acid Frequency | 1 time / 1~3 days / set | ||
Sodium Hypochlorite Frequency | 1 time / 1~3 days / set | ||
Backwash flow rate | 0.5~1.5 times the product water flux | ||
Maintenance Cleaning Chemical Concentration | 0.5%~1% Citric Acid 300~500ppm Sodium Hypochlorite | ||
Recovery cleaning (CIP) method | Alternating internal and external circulation rinsing with citric acid solution and sodium hypochlorite solution | ||
CIP duration (acid cleaning or sodium hypochlorite cleaning) | 90~180min | ||
CIP acid cleaning frequency | 1 time/30~90 days/set | ||
CIP sodium hypochlorite cleaning frequency | 1 time/30~90 days/set | ||
CIP circulation flow rate | 1~3m³/per membrane component | ||
Concentration of recovery cleaning solution | 1%~2% citric acid 1000~3000ppm sodium hypochlorite | ||
Optimal temperature range for each cleaning solution | 20~30℃ | ||
Heating temperature for each cleaning solution | 20~30 |
Size
AD-UF3-HF51:
Unit | L | L1 | L2 | L3 | D | W1 | W2 |
mm | 1860 | 1500 | 1630 | 1820 | 225 | 180 | 342 |
AD-UF3-HF77:
Unit | L | L1 | L2 | L3 | D | W1 | W2 |
mm | 2360 | 2000 | 2130 | 2320 | 225 | 180 | 342 |
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Ultrafiltration Membrane Module
High precision: nominal pore size of 0.03μm, uniform pore size, water turbidity < 0.1 NTU, SDI15 < 2.5; High flux: large channel component structure coupled with high flux membrane fibers, designed flux can reach 120 LMH; High water efficiency: precise fixed-length design, wastewater volume < 5%;
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