4040-Fr Industrial Fouling-Resistant Membrane Reverse Osmosis RO Membrane

• Customization: Available
• Membrane Type: Hollow
• Type: RO
• Model NO.: FROTEC-FR4040, 8040
• Transport Package: in Carton & Pallets
• Specification: 4040, 8040
• Trademark: TANFO
• Origin: Guangzhou
• HS Code: 8421219990
• Production Capacity: 50000PCS/Year

Product Description

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

 

Model	Active Membrane Area ft2(m2)	Stabilized Salt Rejection %	Minimum Salt Rejection %	Permeate Flow Rate gpd(m3/d)
8040FR	400(37)	99.5	99.0	10,500(40)
4040FR	78(7.2)	99.5	99.0	2,050(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

 

Model	A inch(mm)	B inch(mm)	C inch(mm)	D inch(mm)
8040FR	40(1,016)	0	1.125(29)	7.9(201)
4040FR	40(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.