| A m | membrane area (m2) |
| a w | activity of water (-) |
| B w | water vapor permeability (s/m) |
| c f | salt concentration in the feed (kg/m3) |
| c f,0 | initial feed concentration (kg/m3) |
| c p | permeate concentration (kg/m3) |
| c p,distill | salt concentration in the distilled water (kg/m3) |
| c p,leak | salt concentration in the water leakage (kg/m3) |
| c p,net | salt concentration of the water transferred through the membrane (kg/m3) |
| D e | specific gravity of the ethanol (g/cm3) |
| D p | specific gravity of the PVDF material (g/cm3) |
| J v | permeate (water) flux (kg/m2-h) |
| L w | leakage ratio (-) |
| m 1 | mass of the saturated membrane (g) |
| m 2 | mass of the dry membrane (g) |
| p w | vapor pressure (bar) |
| R app | apparent salt rejection (-) |
| R int | intrinsic rejection (-) |
| subscript f | feed |
| subscript p | permeate |
| superscript 0 | pure water |
| x NaCl | mole fraction of NaCl (-) |
| x w | mole fraction of water (-) |
| Δmg | increased mass of the permeate (g) |
| Δpw | vapor pressure difference (bar) |
| Δt | time interval (s) |
| γ | activity coefficient (-) |
| γ w,f | activity coefficient of water in the feed (-) |
| ρ | density of water (kg/m3) |