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    PRODUCT SYSTEM

    2860 dow ultrafiltration membrane on sales - FeaturesThe DOW™ Ultrafiltration (UF) modules are made from high strength, hollow fiber membranes that have excellent features and benefits:• 0.03 µm nominal pore diameter for removal of bacteria, viruses, andparticulates including colloids to protect downstream processessuch as RO•

    2860 dow ultrafiltration membrane on sales

    Features

    The DOW™ Ultrafiltration (UF) modules are made from high strength, hollow fiber membranes that have excellent features and benefits:

    • 0.03 µm nominal pore diameter for removal of bacteria, viruses, and particulates including colloids to protect downstream processes such as RO

    • PVDF polymeric hollow fibers for high strength and chemical resistance allows long membrane life

    • Hydrophilic PVDF fibers for easy cleaning and wettability that help maintain long term performance

    • Outside In flow configuration for high tolerance to feed solids that help reduce the need for pretreatment processes

    • U-PVC housing, helping to eliminate the need for costly pressure vessels

    This module is an ideal choice for systems with capacities greater than 50 m3/hr (220 gpm). The larger, 8 inch diameter module offers the highest effective membrane area of the DOW UF modules, which contributes to a more economical membrane system design. The shorter, 60 inch length module offers higher efficiencies over a wider range of feed water conditions compared to longer length modules.

    DOWTM Ultrafiltration Modules can be used for a wide variety of treatment applications such as surface water, seawater, industrial wastewaters, and secondary effluent wastewater

    Product Specifications


     

    Membrane area

     

    Module volume

    Weight

    (empty/ water filled)

     Model

    Type

     Part#

     m2

     ft2

    Liters

     Gallons

     Kg

     Ibs

     SFP-2860

    Pretreatment

     280933

    51

    549

    35

    9.3

    48/83

    106/183

      SFD-2860

    NSF/ANSI 61 Drinking water

     324168

    51

    549

    35

    9.3

    48/83

    106/183

       Figure 1: SFP and SFD 2860 (8-inch diameter)

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    Figure 2

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    Properties

    Length

    Diameter

    Width

    Units

    L

    L1

    L2

    L3

    D

    W1

    W2

    SI (mm)

    1860

    1500

    1630

    1820

    225

    180

    342

    US (inch)

    73.2

    59.1

    64.2

    71.7

    8.9

    7.1

    13.5

     

    Operating Parameters

                  


    SI units

    US units

    Filtrate Flux @ 25

    40-120 l/m2 / hr

    24-70 gfd

    Flow range

    2.0 – 6.1 m3 /hr

    9.2 – 26.7 gpm

    Temperature

    1-40ºC

    34-104ºF

    Max. inlet module pressure (@ 20)

    6.25 bar

    93.75 psi

    Max. operating TMP

    2.1 bar

    30 psi

    Max operating air scour flow

    12 nm3 /hr

    7.1 scfm

    Max backwash pressure

    2.5 bar

    36 psi

    Operating pH

    2- 11

    NaOCl (max.)

    2,000 mg/L

    TSS (max.)

    100 mg/L

    Turbidity (max.)

    300 ntu

    Particle size (max.)

    300 µ

    Flow configuration

    Outside in, dead end flow

    Expected filtrate turbidity

    ≤0.1 NTU

    Expected filtrate SDI

    ≤2.5

     

    Important information

    Proper start-up of a UF system is essential to prepare the membranes for operating service and to prevent membrane damage. Following the proper start-up sequence also helps ensure that system operating parameters conform to design specifications so that system water quality and productivity goals can be achieved. Before initiating system start-up procedures, membrane pretreatment, installation of the membrane modules, instrument calibration and other system checks should be completed. Please refer to the product technical manual.

    Operation guidelines

    Avoid any abrupt pressure variations during start-up, shutdown, cleaning or other sequences to prevent possible membrane damage. Flush the UF system to remove shipping solution prior to start up. Remove residual air from the system prior to start up. Manually start the equipment. Target a permeate flow of 60% of design during initial operations. Depending on the application, permeate obtained from initial operations should be discarded. Please refer to the product technical manual.

     

     

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