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The choice of the method depends mainly on the level of feed water salinity, source of energy and type of contaminants present.
However, conventional pretreatment (coagulation/filtration) or even the advanced membrane (MF/UF) pretreatment processes which are used to attain the desired level of feed water quality are not capable of preventing fouling completely.
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Pretreatment of field water using ultrafiltration membrane essentially prevents microbial contamination of feed water.
On the other hand, pressure drop and level of the feed water value reduces through time and show good adoption with the measurements.
In particular the test OSU-MASLWR-002 investigated the primary system flow rates and secondary side steam superheat, used to control the facility, for a variety of core power levels and Feed Water (FW) flow rates.
The interaction of feed flow rate, temperature levels, feed water salinity and geometrical module design parameters are quantified and discussed.
The salinity of the water is reduced to an equilibrium level which is typically between 10 and 80% of the feed water salinity (Antia 2017, 2018a, b, c).
The salinity of the water is reduced to an equilibrium level which is typically between 5 and 80% of the feed water salinity (Antia 2015a, b, 2016a, b, 2017, 2018a, b, c).
The DCMD process performance was optimized using a locally designed and fabricated module aiming to maximize the flux at different levels of operating parameters, mainly feed water and coolant inlet temperatures at different temperature differences across the membrane (ΔT).
The temperature of the feed water was 25 °C with pH adjusted at 6 7 for 2000 ppm feed solution of NaCl and at 1 gal/min feed flow rate.
The specific entropy generation of the system could be minimized with lower top brine temperatures, higher operating stages, high completion level of evaporation/condensation processes and lower feed water salinities.
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