8inch RO Membrane for Fouling Resistant Water Furify Treatment

• Customization: Available
• Certification: ISO9001
• Salt Rejection Rate: 99.0%
• Model NO.: FR-8040
• Capacity: 1000
• Active Membrane Area: 78(7.2)/ 400(37)
• Stabilized Salt Rejection: 99.5
• Minimum Salt Rejection: 99.0
• Permeate Flow Rate Gpd: 2,050(7.8)/ 10,500(40)
• Maximum Operating Pressure: 41 Bar(600 Psi)
• Maximum Operating Temperature: 1.0 Bar (15 Psi)
• pH Range, Continuous Operation: 2-11
• Transport Package: Carton
• Specification: 111*13*13 113cm*24cm*25cm
• Trademark: FROTEC
• Origin: China
• Production Capacity: 1000000 Piece/Month

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.