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Industrial 8040-Fr RO Membrane Fouling-Resistant Membrane

China Industrial 8040-Fr RO Membrane Fouling-Resistant Membrane, Find details about China Fouling-Resistant Membrane, Water Filter from Industrial 8040-Fr RO Membrane Fouling-Resistant Membrane

Model NO.
FROTEC-FR4040, 8040
HS Code
8421219990
Model NO.
FROTEC-FR4040, 8040
HS Code
8421219990

FROTEC 8040FR / 4040FR fouling-resistant membrane



FROTEC 8040FR / 4040FR elements can separate salts from water and increase permeability while offering superior salt rejection. They are ideal for use in large-scale industrial and municipal water treatment systems.

FROTEC 8040FR / 4040FR elements can lower the cost of desalination by improving energy efficiency and productivity significantly.
 

Suitable for:


new-built or existing RO systems.
challenging feed water with low quality.
various operating conditions with 4″and 8″elements.


Product Specifications

 
ModelActive Membrane Area
ft2(m2)		Stabilized Salt Rejection
%		Minimum Salt Rejection
%		Permeate Flow
Rate gpd(m3/d)
8040FR400(37)99.599.010,500(40)
4040FR78(7.2)99.599.02,050(7.8)

Test Condition: Feed Water Pressure 1.55MPa (225 psi); Feed Water Temperature 25 °C (77 °F); Feed Water Concentration 2,000 ppm NaCl; Feed Water pH 7; Permeate Recovery 15%.
 

 

Dimensions


Industrial 8040-Fr RO Membrane Fouling-Resistant Membrane
 
ModelA inch(mm)B inch(mm)C inch(mm)D inch(mm)
8040FR40(1,016)01.125(29)7.9(201)
4040FR40(1,016)1.05(26.7)0.75(19)3.9(99)


Operation    Condition
Maximum Operating Pressure                                         41 bar(600 psi)
Maximum Operating Temperature                                   45ºC(113ºF)
Maximum Pressure Drop per Element                            1.0 bar (15 psi)
pH Range, Continuous Operation                                  2-11
pH Range, Chemical Cleaning                                        1-13
Maximum Feed Silt Density Index (SDI15)                       5.0
Free Chlorine Tolerance                                                 < 0.1 ppm
 

Note

1. Permeate flow rates for individual elements may vary ±15%. 2, Membrane active areas may vary ±4%.
3. Stabilized salt rejection is generally achieved after continuous using for 24-48 hours, which depending on feed water qualities and operating conditions.
 

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