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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 />

xvi

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