Dear Mohsan, ...

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Dear Mohsan,

Coagulation-floculation in front of UF to increase the size of particle could be a solution to reduce turbidity. 

Note that UF will not remove dissolved organic material so, Assimilable organic carbon, AOC, and others aliphatic hidrocarbon chains will pass through the membrane, besides this UF isn't a true dissinfection system (although reduce the microorganims level), it means that bio-fouling could appear on your RO membranes after UF.

As an ozone treatment expert I think that a typical DWTP in front of RO membranes is a good solution, so, DAF (for algae removal and bloom barrier) - sand filtration and for dissolved organic material and dissinfection -  O3+BAC+UV in front of  the cartridge filter + RO.

a Pre-oxidation step will be required for metals removal as iron.

For any ozone and UV treatment, please, contact me: cgarcia@newlandentecheurope.com   _src="https://www.newlandentecheurope.com" href="http://www.newlandentecheurope.com">www.newlandentecheurope.com

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Ok, Send me ​your pre ​treatment  ​Complete Design,​ Brief ​Introduction, ​

01, Removal ​Rate, TSS, ​Micro, SDI ​expectation ​result after ​filtration, (​Raw conductivity ​25000) ​

Email: ch_​mohsan91@​hotmail.​com  ​

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