Skip to main content
. 2018 Sep 3;15(9):1913. doi: 10.3390/ijerph15091913
Am active membrane area (m2)
Cp non-condensable heat capacity (J/mol/K)
Cpf feed stream heat capacity (J/kg/K)
Cp,g water (vapour) heat capacity (J/kg/K)
Cp,l water (liquid) heat capacity (J/kg/K)
D pipe diameter (m)
DH hydraulic diameter (m)
ev friction loss factor (dimensionless)
Ef feed pump electrical energy (J)
Er latent heat of condensation (J)
ETotal overall energy requirement (J)
Ev vacuum pump electrical energy (J)
f Darcy’s friction factor (dimensionless)
J permeate flux (kg/m2·h)
L channel length (m)
mf mass flow rate of feed stream (kg/s)
mnc non-condensable flow rate (mol/s)
mp mass flow rate of permeate (kg/s)
MW molecular weight of non-condensable gases (g/mol)
Pin vacuum pump inlet pressure (Pa)
Pout vacuum pump outlet pressure (Pa)
Qc permeate stream cooling energy (J)
Qh feed stream heating energy (J)
Q init one-off initial heating energy (J)
R universal gas constant (J/mol/K)
Re Reynold’s number (dimensionless)
Tfi temperature of feed inlet (K)
Tfo temperature of feed outlet (K)
Tin temperature of vacuum pump inlet stream (K)
Tpc condensation temperature of permeate (K)
Tpi temperature of permeate inlet (K)
Tpo temperature of permeate outlet (K)
TRes temperature of feed reservoir (K)
Tout temperature of vacuum pump outlet stream (K)
u linear velocity of feed stream (m/s)
Vf volumetric flow rate of feed stream (m3/s)
ΔPf pressure drop of pipe due to friction (Pa)
ε surface roughness (m)
β smaller cross section/larger cross section (dimensionless)
γ adiabatic expansion coefficient (dimensionless)
λ latent heat of condensation of water vapour (J/kg)
ρ fluid density (kg/m3)
μ fluid viscosity (Pa.s)
η p1 feed pump efficiency (%)
η p2 vacuum pump efficiency (%)
Subscripts
fi feed inlet
fo feed outlet
pi permeate inlet
po permeate outlet