Page 37 - Separation process engineering
P. 37
μ μ L
H
viscosity of heavy and light phases, Pa·s
μ
m
mixture viscosity, Eq. (13-55), Pa·s
ρ , ρ D
C
densities of continuous and dispersed phases, g/m 3
ρ m
mixture density, Eq. (13-53), g/m 3
ρ m
molar density, mol/m 3
ω
revolutions per second
Chapter 17
a, a j
term in quadratic equations for well-mixed membrane systems, Eqs. (17-10b),
(17-74a), and
â
constant in expression to calculate osmotic pressure, kPa/mole fraction, Eq.
(17-15a)
a′
constant in expression to calculate osmotic pressure, kPa/weight fraction, Eq.
(17-15b)
a i
activities, Eq. (17-51)
A
2
membrane area available for mass transfer, cm or m 2
b, b j
term in quadratic equations for well-mixed membrane systems, Eqs. (17-10c),
(17-74b), and
c, c j
term in quadratic equations for well-mixed membrane systems, Eqs. (17-10d),
(17-74c) and
c
concentration, g solute/L solution
c
out
outlet concentration of solute, g/L
c p