Reverse osmosis membranes

DOW FILMTEC XLE-4040 Membrane Element

Artnumber: XLE-4040
$355
Article: XLE-4040

Dow Filmtec™ XLE-4040 is a high-performance reverse osmosis element with low energy consumption. Suitable for purification of water with medium level of mineralization. It provides high quality water at low operating costs.

The Dow Filmtec™ XLE-4040 membrane element operates at pressure minimal for reverse osmosis, by this reducing energy consumption.

Key advantages

  • Dow Filmtec™ membrane (USA) is the world standard for water purification

  • High energy efficiency due to low operating pressure

  • Large active surface of ​​the element provides higher productivity

  • Automated high-precision production makes it possible to obtain elements with maximum active surface


Membrane type – spiral-wound element with polyamide thin-film composite

Nominal active surface, m2

Operating pressure, bar

Permeate volume, m3/day

Stabilized salt rejection, %

8.1

6.9

9.8

99.0

  1. Permeate consumption and salt (NaCl) rejection are indicated for the following test conditions: 500 mg/L NaCl, 25°C and 15% permeate recovery.  

  2. Flow rates of permeate for every specific element might vary, but will not fluctuate by more than 15% from the indicated values.

Operating conditions

Maximum operating water temperature, °С

45

Maximum operating pressure, bar

41

Maximum pressure drop, bar

0.9

pH range, operational mode

2...11

pH range, chemical cleaning mode

1...13

Maximum feed silt density index (SDI)

SDI < 5

Free chlorine tolerance, mg/L

< 0.1


Before launch of the reverse osmosis system preliminary preparation of the membrane, refill of the elements, adjustment of the devices and other system checks should be performed.

Avoid any major pressure or flow surges inside the spiral-wound elements in the middle of launch, stop, cleaning etc. to avoid risk of damage infliction to the membrane. During the launch it is recommended to gradually switch the system from standstill to operational mode following the steps:

  • gradually increase feed water pressure during 30-60 seconds

  • operational rate of the flows should be developed gradually during 15-20 seconds

  • permeate obtained within the first hour of operation is discharged

Important information

  • After the initial soaking always keep the elements wet.

  • To prevent biofouling during long operation breaks it is recommended to submerge the membrane elements into preservative solutions.

  • Maximum pressure drop along the full length of the housing makes 2.1 bar.