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MBR membrane , as a type of microfiltration membrane, can effectively remove pollutants such as suspended solids and microorganisms from wastewater, producing high-quality purified water. It is widely used in wastewater treatment, industrial wastewater treatment, and water resource recovery, offering excellent water purification performance and space-saving advantages.
Our MBR membranes are made of hollow fiber PVDF membrane with high tensile strength and excellent chemical corrosion resistance. The 0.1 μm pore size provides excellent rejection of suspended solids, bacteria, and viruses. Compared with conventional treatment, SWB MBR modules produce extremely high quality permeate. Due to the high mixed liquor suspended solids (MLSS), SWB MBR modules can greatly reduce the overall treatment plant footprint and annual operation cost.
SWB1V Series Modules
SWB3V Series Module
SWBT Series Module
SWBFT Series Module
SWB1V MBR modules are made with reinforced hollow fiber PVDF membrane. The hollow fibers have high tensile strength with excellent chemical resistance. 0.1μm pore size provides superior rejection rate of suspended solids, bacteria and viruses.Compared with conventional treatment, SWB1V MBR modules produce extremely high quality permeate.Due to the high mixed liquor suspended solids (MLSS), SWB1V MBR modules can greatly reduce the overall treatment plant footprint and annual operation cost.
*Equivalent modules can be customized on customers' request.
Specifications
Module Model | SWB1V4024-10 | SWB1V6024-15 | SWB1V7924-20 |
---|---|---|---|
Effective Membrane Area (m2/ft2) | 10/107.64 | 15/161.46 | 20/215.28 |
Membrane Material | PVDF (with PET supporting layer) | ||
Pore Size (μm) | 0.1 | ||
Fiber I.D./O.D. (mm/inch) | 1.1 / 2.2 | ||
L1 (mm/inch) | 1,000/39.37 | 1,500/59.05 | 2,000/78.74 |
L (mm/inch) | 1,025/40.35 | 1,525/60.04 | 2,025/79.72 |
W (mm/inch) | 480/18.9 | 480/18.9 | 480/18.9 |
W1 (mm/inch) | 620/24.4 | 620/24.4 | 620/24.4 |
W2 (mm/inch) | 591.7/23.30 | 591.7/23.30 | 591.7/23.30 |
I (mm/inch) | 28.3/1.11 | 28.3/1.11 | 28.3/1.11 |
H (mm/inch) | 48/1.89 | 48/1.89 | 48/1.89 |
Permeate Port D | DN20 | ||
End Cap Size d (mm) | φ24 | ||
Filtration Mode | Suction with negative pressure | ||
Design Flux (LMH) | 10–30 | ||
Module Gross Weight (kg/lb) | 4.7/10.36 | 5.8/12.79 | 6.6/14.55 |
Sealing Material | PU | ||
Permeate Collecting Tube Material | ABS | ||
Recommended Flux (L/H) | 100–300 | 150–450 | 250–750 |
Max.△TMP (Mpa/psi) | -0.05/-7.25 | ||
Operation Temp. Range (°C/°F) | 5–40 / 41–104 | ||
Optimal Operation pH Range | 6–9 | ||
Recommended pH Range | 2–10 | ||
Max.Active Chlorine (ppm) | 1,000 | ||
Permeate Turbidity (NTU) | ≤ 0.5 | ||
Permeate SS (mg/L) | ≤ 5 |
Module Model | SWB1V4024-10P | SWB1V6022-15P | SWB1V7924-20P |
---|---|---|---|
Effective Membrane Area (m2/ft2) | 10 | 15 | 20 |
Membrane Material | PVDF (with PET Supporting Layer) | ||
Pore Size (μm) | 0.1 | ||
Fiber O.D. (mm) | 2.2 | ||
L1 (mm) | 610 | 570 | 610 |
L2 (mm) | 950 | 1450 | 1950 |
L3 (mm) | 1025 | 1525 | 2025 |
W (mm) | 46 | 46 | 46 |
Connector | φ27 | φ27 | φ27 |
Filtration Mode | Suction with Negative Pressure | ||
Recommended TMP (Kpa) | 0–35 | ||
Maximum backwash pressure (Kpa) | 70 | ||
Design Flux (L/m2.h, 25 °C) | 15–30 | ||
Backwash Flux (L/m2.h) | 20–50 | ||
Operation Temp. Range (°C) | 5–45 | ||
Recommended pH Range | 2–10 | ||
Aeration (Nm3/m2.h) | Pulse Aeration: 50–75, Perforated aeration: 80–120 | ||
Chemical Cleaning pH Range | 1–12 | ||
Maximum NaClO Tolerance Concentration (mg/L) | 3000 | ||
Permeate Turbidity (NTU) | ≤ 0.8 | ||
Permeate SS (mg/L) | ≤ 5.0 |
Module Model | SWB1V8032-30 |
Membrane Surface Areas (m2/ft2) | 30/322.92 |
Hollow Fiber Material | PVDF (with PET supporting layer) |
Pore Size (μm) | 0.1 |
I.D. / O.D (mm/inch) | 1.1 / 2.2 |
Flow Direction | Outside-in |
L1 (mm/inch) | 2,040/80.31 |
L2 (mm/inch) | 2,000/78.74 |
W (mm/inch) | 825/32.48 |
H (mm/inch) | 42/1.65 |
End Cap d (mm) | DN32 |
Flow Mode | Suction with Negative Pressure |
Flux Design (LMH) | 10–30 |
Sealing Material | PU |
Permeate Collecting Tube Material | ABS |
Operation Flux (L/H) | 300–900 |
Max. △ TMP (Mpa/psi) | -0.05/-7.25 |
Operation Temperature (°C/°F) | 5–40/41–104 |
Optimal Operation pH Range | 6–9 |
Recommended pH Range | 2–10 |
Max. Active Chlorine (ppm) | 1,000 |
Permeate Turbidity (NTU) | ≤ 0.5 |
Permeate SS (mg/L) | ≤ 5 |
Module Model | SWB1V7849-30I |
Membrane Surface Areas (m2/ft2) | 30/322.92 |
Membrane Material | PVDF (with PET Supporting Layer) |
Supporting Rod Material | SS304 |
Pore Size (μm) | 0.1 |
I.D. / O.D. (mm/inch) | 1.1 / 2.2 |
L (mm/inch) | 2,000/78.74 |
W (mm/inch) | 1,250/49.21 |
H (mm/inch) | 32/1.26 |
End Cap d (mm) | φ24 |
Flow Mode | Suction with Negative Pressure |
Flux Design (LMH) | 10–30 |
Module Weight (kg/lb) | 13/28.66 |
Sealing Material | PU |
Permeate Collecting Tube Material | ABS |
Operation Flux (L/H) | 300–900 |
Max. △ TMP (Mpa/psi) | -0.05/-7.25 |
Operation Temperature (°C/°F) | 5–40 / 41–104 |
Optimal Operation pH Range | 6–9 |
Max. Temperature (°C/°F) | 40/104 |
Recommended pH Range | 2–10 |
Max. Active Chlorine (ppm) | 1,000 |
Permeate Turbidity (NTU) | ≤ 0.5 |
Permeate SS (mg/L) | ≤ 5 |
SWB3V modules are made with reinforced hollow fiber PVDF membrane. The hollow fibers have high tensile strength with excellent chemical resistance. 0.03μm pore size provides superior rejection rate of suspended solids, bacteria and viruses.
Compared with conventional treatment, SWB3V modules produce extremely high quality permeate. Due to the high mixed liquor suspended solids (MLSS), SWB3V can greatly reduce the overall treatment plant footprint and annual operation cost.
Specifications
Module Model | SWB3V4024-10 | SWB3V6024-15 | SWB3V7924-20 |
Membrane Surface Areas (m2/ft2) | 10/107.64 | 15/161.46 | 20/215.28 |
Membrane Material | PVDF(with PET supporting layer) | ||
Pore Size (μm) | 0.03 | 0.03 | 0.03 |
Fiber I.D. / O.D. (mm/inch) | 1.1 / 2.2 | ||
L1 (mm/inch) | 1,000/39.37 | 1,500/59.05 | 2,000/78.74 |
L (mm/inch) | 1,025/40.35 | 1,525/60.04 | 2,025/79.72 |
W (mm/inch) | 480/18.9 | 480/18.9 | 480/18.9 |
W1 (mm/inch) | 620/24.4 | 620/24.4 | 620/24.4 |
W2 (mm/inch) | 591.7/23.30 | 591.7/23.30 | 591.7/23.30 |
I (mm/inch) | 28.3/1.11 | 28.3/1.11 | 28.3/1.11 |
H (mm/inch) | 48/1.89 | 48/1.89 | 48/1.89 |
Permeate Port D | DN20 | ||
End Cap Size d (mm) | φ24 | ||
Filtration Mode | Suction with Negative Pressure | ||
Design Flux (LMH) | 10–30 | ||
Module Gross Weight (kg/lb) | 4.7/10.36 | 5.8/12.79 | 6.6/14.55 |
Sealing Material | PU | ||
Permeate Collecting Tube Material | ABS | ||
Recommended Flux (L/H) | 100–300 | 150–450 | 250–750 |
Max. △ TMP (Mpa/psi) | -0.05/-7.25 | ||
Operation Temperature (°C/°F) | 5–40 / 41–104 | ||
Optimal Operation pH Range | 6–9 | ||
Recommended pH Range | 2–10 | ||
Max. Active Chlorine (ppm) | 1,000 | ||
Permeate Turbidity (NTU) | ≤ 0.2 | ||
Permeate SDI | ≤ 5 |
Module Model | SWB3V8633-31S | SWB3V8633-34S | SWB3V8633-40S |
Effective Membrane Area (m2) | 31.6 | 34.4 | 40.9 |
Membrane Material | PVDF (with PET supporting layer) | ||
Pore Size (μm) | 0.03 | ||
Fiber I.D. / O.D. (mm) | 1.1 / 2.2 | ||
L (mm) | 2,198 | ||
W (mm) | 844 | ||
H (mm) | 49 | ||
Permeate Collecting Tube Material | ABS | ||
Sealing Material | PU | ||
Operation Temperature (°C) | 5–40 | ||
Filtration Mode | Suction with Negative Pressure | ||
Design Flux (LMH) | 10–30 | ||
TMP Range (Kpa) | -55 Kpa to +55 Kpa | ||
Recommended pH Range | 2–10 | ||
Turbidity (NTU) | ≤ 0.2 | ||
Permeate SDI | ≤ 5 |
SWBT PTFE-MBR modules are made of highly hydrophilic PTFE membrane fiber, which have excellent chemical resistance and high hydrophilicity. With 0.1 μm filtration pore size, it has excellent retention effects on impurities such as solid particles, colloidal suspensions, and bacteria. Compared to traditional treatment processes and PVDF MBR membrane products, SWBT PTFE-MBR modules have the advantages of small footprint, better effluent quality, longer service life, and stronger chemical cleaning tolerance.
Specifications
Module Model | SWBT6132-25 | SWBT8632-36 | SWBT12532-53 |
Membrane Material | Permannet Hydrophilicity PTFE | ||
Pore Size (μm) | 0.1 | ||
Fiber I.D. / O.D. (mm) | 1/2.3 | ||
Effective Membrane Area (m2) | 25 | 36 | 53 |
Overall dimension (mm) | 825 × 46 × 1,560 | 825 × 46 × 2,200 | 825 × 46 × 3,200 |
Permeate Outlet | DN32 | ||
Housing Material | ABS | ||
Sealant | Epoxy Resin | ||
Operation Temperature (°C) | 4–45 | ||
Recommended pH Range | 0–14 | ||
MLSS (mg/L) | 5,000–20,000 | ||
Design Flux (LMH) | 10–40 | ||
Backwash Flux (LMH) | 1.5–2 multiple to design flux | ||
Max. TMP Range (Kpa) | 60 | ||
Max. Backwash pressure (Kpa) | 100 | ||
Aeration (Nm3/m2*h) | 50–100 |
SWBFT PTFE-MBR Flat Sheet Modules are made of highly hydrophilic PTFE membrane fiber, which have excellent chemical resistance and high hydrophilicity. With 0.2μm filtration pore size, it has excellent retention effects on impurities such as solid particles, colloidal suspensions, and bacteria. Compared to traditional treatment processes and PVDF MBR membrane products, SWBFT PTFE-MBR Flat Sheet modules have the advantages of small footprint, better effluent quality, longer service life, and stronger chemical cleaning tolerance.
Specifications
Membrane Elements Model | SWBFT3919-08 | SWBFT6819-15 |
Effective Membrane Area (m2) | 0.8 | 1.5 |
Size: W × H × D (mm) | 490 × 1,000 × 7 | 490 × 1,750 × 7 |
Weight (kg) | 3.2 | 5.5 |
Pore Diameter (μm) | 0.2 | |
Membrane Material | PTFE | |
Lining Plate Material | ABS | |
Filtrated Mode | Negative Pressure Suction, Continuous Aeration | |
Flux | 300–600 | 600–900 |
Aeration Volume | ≥ 10 | ≥ 10 |
pH | 1–14 | |
Permeate Turbidity (NTU) | ≤ 0.2 | |
Permeate SS (mg/L) | ≤ 1 |
The MBR membrane system consists of two stages: biological reaction and membrane separation. When the wastewater enters the bioreactor, microorganisms convert pollutants such as organic matter, nitrogen, and phosphorus into microorganisms and gas through metabolic activities.
The wastewater treated in the bioreactor enters the membrane separation stage. The small pore size of the MBR membrane retains pollutants such as suspended solids, microorganisms, and solid particles on the membrane surface, forming concentrated sludge. Clean water molecules pass through the membrane pores and flow out of the MBR membrane system, producing high-quality purified water.
Here are product catalogue and data sheet for your reference. more information just contact us.