mass transfer in multiphase systems - Greenleaf University
mass transfer in multiphase systems - Greenleaf University
mass transfer in multiphase systems - Greenleaf University
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NOMENCLATURE a<br />
a,b, etc.<br />
Parameter <strong>in</strong> Sherwood number, other constants<br />
a Bubble specific surface area, L 2 /L 3<br />
a s Solid specific surface area, L 2 /M<br />
A<br />
Area, L 2 , Component A<br />
c Concentration, m/L 3 or M/L 3<br />
C A Concentration of chemical A, m/L 3 or M/L 3<br />
i1<br />
C A<br />
i2<br />
C A<br />
s*<br />
C A<br />
v*<br />
C A<br />
d p<br />
D<br />
d B , D B<br />
Interface concentration of A on the solid side, m/L 3 or M/L 3<br />
Interface concentration of A on the liquid side, m/L 3 or M/L 3<br />
Nonexistent concentration of A on with<strong>in</strong> the solid phase, m/L 3 or M/L 3<br />
Nonexistent concentration of A on with<strong>in</strong> the gas phase, m/L 3 or M/L 3<br />
Particle mean diameter, L<br />
Diameter or characteristic length, L<br />
Bubble diameter, L<br />
D Aw , D L Diffusivity of component A <strong>in</strong> water, L 2 /t<br />
D AB Diffusivity of component A <strong>in</strong> component B, L 2 /t<br />
f oc<br />
Fr<br />
Fraction organic carbon <strong>in</strong> sludge<br />
Froude number<br />
g Gravity, L/t 2<br />
H A Henry’s Law constant b for component A, L 3 -F/L 2 /m<br />
a Any consistent set of units except for dimensional equations is acceptable. The superscripts on concentrations<br />
<strong>in</strong>dicate phase or other <strong>in</strong>formation and are not powers. Units follow the standard FLMTt system with the exception<br />
of m for moles.<br />
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