Cost of RO Membrane 4040 Frotec Manufacturer for RO Plant

China Cost of RO Membrane 4040 Frotec Manufacturer for RO Plant, Find details about China Cost of RO Membrane, RO Membrane 4040 from Cost of RO Membrane 4040 Frotec Manufacturer for RO Plant

Model NO.
4040
Max Working Pressure
600psi (4.14MPa)
Max Feedwater Temperature
45°c
Max Feedwater Sdl
5.0
Free Chlorine Concentration of Feedwater
0.1mg/L
pH Range of Feedwater During Continuous
3-10
pH Range of Feedwater During Chemical Cl
2-12
Trademark
FROTEC
Transport Package
Carton or Pallet
Specification
4040
Origin
Made in China
HS Code
8421999090
Model NO.
4040
Max Working Pressure
600psi (4.14MPa)
Max Feedwater Temperature
45°c
Max Feedwater Sdl
5.0
Free Chlorine Concentration of Feedwater
0.1mg/L
pH Range of Feedwater During Continuous
3-10
pH Range of Feedwater During Chemical Cl
2-12
Trademark
FROTEC
Transport Package
Carton or Pallet
Specification
4040
Origin
Made in China
HS Code
8421999090

FROTEC ULP-8040 / ULP-4040 low pressure membrane



FROTEC ULP-8040 / ULP-4040 elements can produce high-quality water at low operating costs. They are ideal for use in large-scale industrial and municipal water treatment systems.

FROTEC ULP-8040 / ULP-4040 elements can lower the operating pressure by 40%.

 

Suitable for:


new-built or existing RO systems.
municipal and industrial water demineralization system.
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)
ULP-8040400(37)99.399.011,500(44)
ULP-404078(7.2)99.399.02250(8.7)

Test Condition: Feed Water Pressure 1.03MPa (150 psi); Feed Water Temperature 25 °C (77 °F); Feed Water Concentration 2,000 ppm NaCl; Feed Water pH 7; Permeate Recovery 15%.
 

 

Dimensions

 Cost of RO Membrane 4040 Frotec Manufacturer for RO Plant
 
ModelA inch(mm)B inch(mm)C inch(mm)D inch(mm)

ULP-8040
40(1,016)01.125(29)7.9(201)

ULP-4040
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.
 
 

FROTEC BW-8040 / BW-4040 high pressure membrane



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


 

Suitable for:


new-built or existing RO systems.
high quality permeate while minimizing unit cost.
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)
BW-8040400(37)99.599.010,500(40)
BW-404078(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

Cost of RO Membrane 4040 Frotec Manufacturer for RO Plant


 
ModelA inch(mm)B inch(mm)C inch(mm)D inch(mm)
BW-804040(1,016)01.125(29)7.9(201)
BW-404040(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.