Membrane distillation
(MD) is a thermal technology for the desalination
process that requires a hydrophobic microporous membrane to ensure
that the membrane can maintain the liquid–vapor interface.
This work aims to enhance the water permeation flux of the previously
coated membrane by modifying the surface of the polytetrafluoroethylene
hollow fiber (PTFE HF) membrane with a selected non-solvent such as
acetone, cyclohexanone, and ethanol in low-density polyethylene as
a polymeric coating solution. However, the modification using acetone
and cyclohexanone solvents was unsuccessful because a reduction in
membrane hydrophobicity was observed. The modified PTFE HF membrane
with ethanol content exhibits high wetting resistance with a high
water contact angle, which can withstand pore wetting during the direct
contact MD process. Since MD operates under a lower operating temperature
range (50–90 °C) compared to the conventional distillation,
we herein demonstrated that higher flux could be obtained at 7.26
L m–2 h–1. Thus, the process is
economically feasible because of lower energy consumption. Performance
evaluation of the modified PTFE HF membrane showed a high rejection
of 99.69% for sodium chloride (NaCl), indicating that the coated membrane
preferentially allowed only water vapor to pass through.